CN105251320A - Centrifugal dehumidifier as well as dehumidifying method and application of centrifugal dehumidifier - Google Patents
Centrifugal dehumidifier as well as dehumidifying method and application of centrifugal dehumidifier Download PDFInfo
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- CN105251320A CN105251320A CN201510754804.5A CN201510754804A CN105251320A CN 105251320 A CN105251320 A CN 105251320A CN 201510754804 A CN201510754804 A CN 201510754804A CN 105251320 A CN105251320 A CN 105251320A
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Abstract
The invention belongs to the technical field of light chemical machinery of food, and relates to a centrifugal dehumidifier as well as a dehumidifying method and application of a centrifugal dehumidifier. The centrifugal dehumidifier comprises a separated conical cylinder (2), a top cylinder and a collector, wherein the top cylinder consists of an outer cylinder (1), an air inlet pipe (4) and an inner cylinder (3); the collector consists of an automatic drain valve (5) and a water storage hopper (6); the large opening end of the separated conical cylinder (2) is connected with the outer cylinder (1) of the top cylinder, and the conical opening end is connected with the automatic drain valve (5) of the collector; the outlet end of the automatic drain valve (5) is connected with the water storage hopper (6); the air inlet pipe (4) is arranged on the side surface of the upper part of the outer cylinder (1) along the tangential direction of the cylinder, cooling devices are arranged inside or outside the outer cylinder (1) and the separated conical cylinder (2), and are provided with cooling medium inlets and cooling medium outlets. The device adopts the centrifugal separator with cooling wall surfaces so as to have obvious dehumidifying effect on high-humidity air, and can be used for dehumidification of food processing workshops and rooms.
Description
Technical field
The invention belongs to food light industry field of mechanical technique, be specifically related to a kind of centrifugal dehumidifier and dehumanization method thereof and application.
Background technology
It is unit operations common in food processing that air humidity regulates, and has material impact to food quality.Humidity control method common at present has phase transformation to dehumidify, mixes the modes such as dehumidifying and adsorption and dehumidification.
Such as Chinese utility model patent authorization document CN203147928U discloses cooled dehumidifier unit between a kind of food car, the principle of this equipment utilization phase transformation dehumidifying, primarily of having the body shell of air inlet and gas outlet, evaporimeter, compressor, condenser, expansion valve and centrifugal blower composition.This cooling phase transformation dehydrating unit often causes heat-transfer area to cross cold frost, thus adds heat transmission resistance, dehumidification rate is declined, and when dehumidifier works in low temperature environment, also will carry out intermittence defrosting, have impact on the operating efficiency of dehumidifier.
Rotary dehumidifier make use of the principle of adsorption and dehumidification, its agent structure is a rotating cellular Dehumidifying rotary wheel, the corrugated media being loaded with hygroscopic agent is filled with in runner, this medium contacts with humid air and reduces the water content in humid air in dehumidifying district, then renewing zone makes in adsorbent moisture evaporating and dewatering by high temperature is entered, to reduce the water content of hygroscopic agent, improve its water absorbing capacity, then enter dehumidifying district carry out circulation continuous dehumidifying.The problems such as this equipment is only suitable for the dehumidifying compared with low relative humidity situation, and it is large to there is operation energy consumption, and runner service life is short.
Direct mixing dehumidifying is that air lower for relative humidity is directly contacted mixing with humid air, and this method is energy-conservation, but affects greatly by air humidity, and moisture removal is limited.
Summary of the invention
The object of the invention is to overcome existing dehumidifier inefficiency, be only suitable for the technical deficiency such as northern area of lower air humidity dehumidifying, provide a kind of to humid air particularly damp atmosphere (as southern china) carry out the centrifugal dehumidifier of efficient dehumidifying.Dehumidifier of the present invention adopts the whizzer with cooling wall, by dehumidification by condensation, and the principle utilizing the density ratio air of moisture in humid air much larger, under the influence of centrifugal force, make both be separated, obtain the dry air that relative humidity is lower.The present invention is particularly evident for the effect on moisture extraction of damp atmosphere, can reduce dehumidifying energy consumption simultaneously.
The present invention is achieved through the following technical solutions:
A kind of centrifugal dehumidifier, comprises separation cone cylinder, top cylinder and collector.It is characterized in that: described top cylinder is made up of outer cylinder, air inlet pipe and inner cylinder; Described collector is made up of automatic drain valve and water storage bucket; The big opening end of described separation cone cylinder is connected with the outer cylinder of top cylinder, and cone mouth end is connected with the automatic drain valve of collector; The port of export of described automatic drain valve is connected with water storage bucket; Described outer cylinder upper side is provided with air inlet pipe along cylindrical shell tangential direction, and the inside/outside portion of described outer cylinder and separation cone cylinder is provided with cooling device, is provided with cooling medium inlet and cooling medium outlet in described cooling device.
Described cooling device or for being arranged on the chuck outside outer cylinder and separation cone cylinder.
Described cooling device or for being arranged on the cold fluid case outside outer cylinder and separation cone cylinder.
Described cooling device or for being arranged on the built-in coil pipe in outer cylinder and separation cone cylinder.
Described cooling device or for being arranged on the external coil pipe outside outer cylinder and separation cone cylinder.
Described outer cylinder diameter is greater than inner cylinder, and described inner cylinder is connected with discharge duct.
The total height of described outer cylinder and separation cone cylinder is greater than the diameter of outer cylinder.
Centrifugal dehumidifier described in employing carries out the method dehumidified, and it is characterized in that, it is as follows that described method comprises step:
1) pass into cooling medium in cooling device, coolant temperature is designated as T
1;
2) humid gas is entered in separation cone cylinder by outer cylinder by air inlet pipe, forms the spiral air flow of movement bottom separation cone cylinder, and the moisture in humid gas forms condensate liquid at separation cone tube wall surface, and described humid gas temperature is designated as T
2;
3) described step 2) condensate liquid enter in collector through tube connector, and air-flow helically rises near separation cone cylinder central shaft, draws, thus obtains dry gas, complete the dehumidifying of air through inner cylinder;
According to following formulae discovery: T
2– T
1>=2 DEG C, cooling medium is liquid or gas.
The application of described centrifugal dehumidifier in air condition adjustment and food drying.
In order to adapt to different processing needs, apparatus of the present invention can match some temperature control systems, comprise cooling-water machine, the mechanical, electrical subflow gauge of Temperature and Humidity Control, heat exchanger etc., these outsourcing devices or parts can obtain from being purchased channel, thus the humiture requirement of producing required air can be reached, those skilled in the art can implement the present invention very easily by existing handbook and document.
The invention has the beneficial effects as follows:
Device of the present invention adopts the whizzer with cooling wall, and the effect on moisture extraction for damp atmosphere (such as southern area of China) is particularly evident.Because the present invention dehumidifies to food processing shop based on the principle of centrifugation, thus can reduce dehumidifying energy consumption, improve dehumidification rate.
Accompanying drawing explanation
Fig. 1: be general structure schematic diagram of the present invention.
Fig. 2: be the top view of Fig. 1.
Fig. 3: the cooling device structural representation in the embodiment of the present invention 2.
Fig. 4: the structural representation of the embodiment of the present invention 3.
Fig. 5: the structural representation of the embodiment of the present invention 4.
Fig. 6: the dehumidifying flow chart of the embodiment of the present invention 6.
Wherein: 1-outer cylinder, 2-separation cone cylinder, 3-inner cylinder, 4-air inlet pipe, 5-automatic drain valve, 6-water storage bucket, 7-chuck, 8-import, 9-exports, 10-cold fluid case, 11-first import, 12-first exports, 13-second import, the built-in coil pipe of 14-, 15-second exports, 16-triple feed inlet, the external coil pipe of 17-, 18-the 3rd exports.
Detailed description of the invention
Further illustrate the present invention below in conjunction with embodiment, but the scope of protection of present invention is not limited to the scope of embodiment statement.
Embodiment 1 (comprising jacket type cooling device)
Below in conjunction with accompanying drawing, device of the present invention and application are described in detail.
As shown in Fig. 1, Fig. 2, a kind of centrifugal dehumidifier, comprises separation cone cylinder 2, top cylinder and collector.It is characterized in that: described top cylinder is made up of outer cylinder 1, air inlet pipe 4 and inner cylinder 3; Described collector is made up of automatic drain valve 5 and water storage bucket 6; The big opening end of described separation cone cylinder 2 is connected with the outer cylinder 1 of top cylinder, and cone mouth end is connected with the automatic drain valve 5 of collector; The port of export of described automatic drain valve 5 is connected with water storage bucket 6; Described outer cylinder 1 upper side is provided with air inlet pipe 4 along cylindrical shell tangential direction, and the outside of described outer cylinder 1 and separation cone cylinder 2 is provided with cooling device, and described cooling device is provided with cooling medium inlet 8 and cooling medium outlet 9.
Described cooling device is be arranged on the chuck 7 outside outer cylinder 1 and separation cone cylinder 2.
Described outer cylinder 1 diameter is greater than inner cylinder 3, and described inner cylinder 3 is connected with discharge duct.
Embodiment 2 (comprising immersion cooling device)
As shown in Figure 3, a kind of centrifugal dehumidifier, comprises separation cone cylinder 2, top cylinder and collector.It is characterized in that: described top cylinder is made up of outer cylinder 1, air inlet pipe 4 and inner cylinder 3; Described collector is made up of automatic drain valve 5 and water storage bucket 6; The big opening end of described separation cone cylinder 2 is connected with the outer cylinder 1 of top cylinder, and cone mouth end is connected with the automatic drain valve 5 of collector; The port of export of described automatic drain valve 5 is connected with water storage bucket 6; Described outer cylinder 1 upper side is provided with air inlet pipe 4 along cylindrical shell tangential direction, and the outside of described outer cylinder 1 and separation cone cylinder 2 is provided with cooling device, and described cooling device is provided with cooling medium inlet 11 and cooling medium outlet 12.
Described cooling device is be arranged on the cold fluid case 10 outside outer cylinder 1 and separation cone cylinder 2.
Described outer cylinder 1 diameter is greater than inner cylinder 3, and described inner cylinder 3 is connected with discharge duct.
Embodiment 3 (comprising built-in coil type cooling device)
As shown in Figure 3, a kind of centrifugal dehumidifier, comprises separation cone cylinder 2, top cylinder and collector.It is characterized in that: described top cylinder is made up of outer cylinder 1, air inlet pipe 4 and inner cylinder 3; Described collector is made up of automatic drain valve 5 and water storage bucket 6; The big opening end of described separation cone cylinder 2 is connected with the outer cylinder 1 of top cylinder, and cone mouth end is connected with the automatic drain valve 5 of collector; The port of export of described automatic drain valve 5 is connected with water storage bucket 6; Described outer cylinder 1 upper side is provided with air inlet pipe 4 along cylindrical shell tangential direction, and the inside of described outer cylinder 1 and separation cone cylinder 2 is provided with cooling device, and described cooling device is provided with cooling medium inlet 13 and cooling medium outlet 15.
Described cooling device is be arranged on the built-in coil pipe 14 in outer cylinder 1 and separation cone cylinder 2.
Described outer cylinder 1 diameter is greater than inner cylinder 3, and described inner cylinder 3 is connected with discharge duct.
Embodiment 4 (comprising external coil type cooling device))
As shown in Figure 3, a kind of centrifugal dehumidifier, comprises separation cone cylinder 2, top cylinder and collector.It is characterized in that: described top cylinder is made up of outer cylinder 1, air inlet pipe 4 and inner cylinder 3; Described collector is made up of automatic drain valve 5 and water storage bucket 6; The big opening end of described separation cone cylinder 2 is connected with the outer cylinder 1 of top cylinder, and cone mouth end is connected with the automatic drain valve 5 of collector; The port of export of described automatic drain valve 5 is connected with water storage bucket 6; Described outer cylinder 1 upper side is provided with air inlet pipe 4 along cylindrical shell tangential direction, and the outside of described outer cylinder 1 and separation cone cylinder 2 is provided with cooling device, and described cooling device is provided with cooling medium inlet 16 and cooling medium outlet 18.
Described cooling device is be arranged on the external coil pipe 17 in outer cylinder 1 and separation cone cylinder 2.
Described outer cylinder 1 diameter is greater than inner cylinder 3, and described inner cylinder 3 is connected with discharge duct.
Embodiment 5: effect on moisture extraction compares
In order to verify embodiments of the present invention, the present embodiment has carried out the contrast test of effect on moisture extraction to the dehumidifier of embodiments of the invention 1-4, and result of the test is as described below.
Technical conditions:
The state of humid air is:
Damp-heat air temperature 60 C, relative humidity 85%, flow is 1000kg/h.
Dehumidifying medium parameter:
5 DEG C of running water coolings, flow is 1000kg/h.
See Fig. 1, Fig. 3-Fig. 5, damp-heat air is transported to the whizzer of band cooling wall via gas transmission pipeline, (whizzer main body adopts uniform sizes, and its size is as follows: air inlet height 0.25m tangentially to enter whizzer by air inlet pipe 4 respectively; Air scoop width 0.125m; Outer cylinder diameter 0.5m; Leakage fluid dram diameter 0.125m; Outer cylinder height 1.0m; Inner cylinder length 0.165m; Inner cylinder diameter 0.25m), and enter whizzer main body downwards twist along cylindrical shell; Cooling water enters through the upper interface of chuck (7), cold fluid case (10), built-in coil pipe (14), external coil pipe (17), and lower interface is discharged.In the process, in humid air, steam is caught a cold condensation, and drop is thrown toward wall under centrifugal action, and under gravity, falls to flowing out in water storage bucket along being separated separation cone cylinder inwall.Air after dehumidifying is discharged via inner cylinder (3).
Adopt the dehumidifier in embodiment 1-4 to carry out dehumidifying experiment respectively, the state parameter of dry air after record dehumidifying, effect on moisture extraction is as shown in table 1 separately for it.As shown in Table 1, use the dehumidifier of built-in coiled (embodiment 3) cooling wall, its effect on moisture extraction is best, is secondly the dehumidifier using immersion (embodiment 2), jacket type (embodiment 1) and external coiled (embodiment 4) cooling wall.
Table 1 four kinds of different structure whizzers are to the effect of the effect on moisture extraction of dehumidification system
Embodiment 6: cooling medium is selected
The present embodiment carries out the contrast of the effect on moisture extraction of different cooling fluid for the external coiled cooling wall dehumidifier (see Fig. 5) in embodiment 4.
Technical conditions:
The state of humid air is:
Damp-heat air temperature 60 C, relative humidity 85%, flow is 1000kg/h.
Except humid medium and parameter:
5 DEG C of running water, or the salt solution of-10 DEG C (sodium chloride concentration is 26.3%), or the ethanol of-20 DEG C (concentration is 30%), flow is 1000kg/h.
After record dehumidifying, the state parameter of dry air, adopts the effect on moisture extraction of different cooling medium in table 2.As shown in Table 2, best as the effect on moisture extraction of cooling medium using-20 DEG C of ethanol, be secondly-10 DEG C of salt solution and 5 DEG C of cold water successively.The results are shown in Table 2.
The effect on moisture extraction of table 2 three kinds of different cooling mediums
Embodiment 7: effect on moisture extraction
The present embodiment carries out the effect on moisture extraction contrast of different humiture air condition with jacket type cooling wall dehumidifier (see Fig. 1) of the present invention, and the size of main body of whizzer is as embodiment 3.
Technical conditions:
The state of humid air is:
Damp-heat air temperature 60 C, relative humidity 85%, flow is 1000kg/h.
Dehumidifying medium parameter: the salt solution of-10 DEG C, flow is 1000kg/h.
The state parameter of dry air after record dehumidifying, to the effect on moisture extraction of different humiture air condition in table 3.As shown in Table 3, the effect on moisture extraction of dehumidifier of the present invention to the air of low temperature and high humidity is better.The results are shown in Table 3.
Table 3 is to the effect on moisture extraction of different air condition
Note: the import relative humidity-outlet relative humidity of humidity change=humid air
Embodiment 9: dehumidifier size Selection:
The present embodiment, for jacket type cooling wall dehumidifier (see Fig. 1) of the present invention, designs different sizes respectively.
Technical conditions:
The state of humid air: damp-heat air temperature 60 C, relative humidity 85%, flow is 1000kg/h.
Except humid medium and parameter: 5 DEG C of running water, flow is 1000kg/h.
Drum diameter D beyond whizzer
cfor basic size (see Fig. 1 and table 4) designs.The dehumidifier of application 3 kinds of different size whizzers, its effect on moisture extraction is in table 5, as shown in Table 5, adopt the dehumidification system effect on moisture extraction of the jacket type whizzer of No. 1 size of main body best, this is because the barrel diameter of No. 1 whizzer is minimum, and in " slender type ", and whizzer diameter is less, can the critical grain size of separating particles less, separative efficiency is higher.Meanwhile, suitable cylindrical shell height also ensure that and the time of staying of drop is beneficial to separation, reduces reentrainment.Implementation result is in table 4, table 5.
Table 4 three kinds of whizzer agent structure size design
Table 4 illustrates:
(1) size Chinese and English letter representation: a-air inlet height; B-air scoop width; D
c-outer cylinder diameter; D
d-leakage fluid dram diameter; H-total height; H
c-outer cylinder height; L-inner cylinder length; D
0-inner cylinder diameter; Dimensional units: m.
(2) whizzer in table 5: No. 1, No. 2, No. 3 external coiled whizzers representing different size respectively.
The effect on moisture extraction of table 5 different size whizzer compares
Table 5 illustrates: humid air temperature 60 C, relative humidity 85%.Cold fluid flow velocity 10m/s.
The application of embodiment 9 dehumidifier of the present invention
Dehumidifier of the present invention can independently use, and dehumidifies to damp atmosphere, and also can connect with cooled dehumidifier unit or rotary dehumidifier uses, and is applied to dehumidify field widely.
The present embodiment to be connected with cooled dehumidifier unit for jacket type cooling wall dehumidifier (see Fig. 1) of the present invention and is used, and be applied in the drying processing of several typical food, dehumidifying flow chart is shown in Fig. 6.Wet stock to be dried is placed in hothouse, provides heat through dry air, takes away steam.Dry air drying room absorbs material moisture, relative humidity raises, enter in dehumidifier of the present invention, humid air air humidity and temperature reduce, enter surface cooler (i.e. cooled dehumidifier unit) again, the dry air after dehumidifying enters heat exchanger again, and the drying-air temperature obtained raises, relative humidity declines, and returns hothouse.
Table 6 the present invention is to the effect on moisture extraction of humid air in several typical food dry run
Previous process, the method for the processing of several typical food listed in table 6 manufacture with reference to existing document.This table is the process entering the drying stage based on the food semi-finished product obtained after pre-treating technology, and test data only records the parameters in drying stage, the results are shown in Table 5.As shown in Table 5, apply dehumidifier of the present invention and connect with cooled dehumidifier unit and use, can dehumidify to the damp atmosphere produced in processing, reach the parameter and standard that machining needs, save energy consumption.
The above embodiments are only the preferred technical solution of the present invention, and should not be considered as restriction of the present invention, and the embodiment in the application and the feature in embodiment, when not conflicting, can be combined mutually.The technical scheme that protection scope of the present invention should be recorded with claim, the equivalents comprising technical characteristic in the technical scheme of claim record is protection domain.Namely the equivalent replacement within the scope of this improves, also within protection scope of the present invention.
Claims (9)
1. a centrifugal dehumidifier, comprises separation cone cylinder (2), top cylinder and collector; It is characterized in that: described top cylinder is made up of outer cylinder (1), air inlet pipe (4) and inner cylinder (3); Described collector is made up of automatic drain valve (5) and water storage bucket (6); The big opening end of described separation cone cylinder (2) is connected with the outer cylinder (1) of top cylinder, and cone mouth end is connected with the automatic drain valve (5) of collector; The port of export of described automatic drain valve (5) is connected with water storage bucket (6); Described outer cylinder (1) upper side is provided with air inlet pipe (4) along cylindrical shell tangential direction, the inner or outer portion of described outer cylinder (1) and separation cone cylinder (2) is provided with cooling device, and described cooling device is provided with cooling medium inlet and cooling medium outlet.
2. centrifugal dehumidifier according to claim 1, is characterized in that: described cooling device is the chuck (7) being arranged on outer cylinder (1) and separation cone cylinder (2) outside.
3. centrifugal dehumidifier according to claim 1, is characterized in that: described cooling device is the cold fluid case (10) being arranged on outer cylinder (1) and separation cone cylinder (2) outside.
4. centrifugal dehumidifier according to claim 1, is characterized in that: described cooling device is arranged on the built-in coil pipe (14) in outer cylinder (1) and separation cone cylinder (2).
5. centrifugal dehumidifier according to claim 1, is characterized in that: described cooling device or for being arranged on outer cylinder (1) and separation cone cylinder (2) external coil pipe (17) outward.
6. centrifugal dehumidifier according to claim 1, is characterized in that: described outer cylinder (1) diameter is greater than inner cylinder (3), and described inner cylinder (3) is connected with discharge duct.
7. centrifugal dehumidifier according to claim 1, is characterized in that: the total height of described outer cylinder (1) and separation cone cylinder (2) is greater than the diameter of outer cylinder (1).
8. be exclusively used in the dehumanization method of the centrifugal dehumidifier described in any one of claim 1-7, it is characterized in that, described method comprises the steps:
1) in cooling device, cooling medium is passed into, if coolant temperature is T
1;
2) humid gas is entered in separation cone cylinder by outer cylinder by air inlet pipe, forms the spiral air flow of movement bottom separation cone cylinder, and the moisture in humid gas forms condensate liquid, if described humid gas temperature is T at separation cone tube wall surface
2;
3) by step 2) condensate liquid enter in collector through automatic drain valve, and air-flow helically rises near separation cone cylinder central shaft, draws, thus obtains dry gas, complete the dehumidifying of air through inner cylinder;
Described T
2– T
1>=2 DEG C, cooling medium is liquid or gas.
9. the application of the centrifugal dehumidifier described in any one of claim 1-7 in air condition adjustment and food drying.
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Cited By (6)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN105768205A (en) * | 2016-05-11 | 2016-07-20 | 常德烟草机械有限责任公司 | Method and device for adjusting and controlling temperature of circulating air flow in fluidized bed |
| CN106178851A (en) * | 2016-08-15 | 2016-12-07 | 宁波德泰化学有限公司 | A kind of centrifugal classification dehydrating unit |
| CN106268200A (en) * | 2016-08-15 | 2017-01-04 | 宁波德泰化学有限公司 | A kind of classification dehydrating unit |
| WO2019067849A1 (en) * | 2017-09-29 | 2019-04-04 | Bendix Commercial Vehicle Systems Llc | Effluent processing apparatus and method for a vehicle air brake charging system |
| CN111790240A (en) * | 2019-11-05 | 2020-10-20 | 山东建筑大学 | Multifunctional negative pressure type dehumidifying and heat exchanger |
| CN111841161A (en) * | 2020-07-29 | 2020-10-30 | 濮阳市盛源能源科技股份有限公司 | Gas-liquid separation device and pressure removal reaction kettle |
Citations (6)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| GB627838A (en) * | 1946-02-26 | 1949-08-17 | Sutcliffe Speakman And Company | Improvements relating to the continuous distillation of solvent or volatile liquids |
| CN2131594Y (en) * | 1992-07-20 | 1993-05-05 | 邓国桢 | Air drying machine |
| CN1715536A (en) * | 2004-07-02 | 2006-01-04 | 三星电子株式会社 | Cyclone type condenser and have the washing/drying machine of described condenser |
| CN202146635U (en) * | 2011-04-27 | 2012-02-22 | 安徽省皖北药业股份有限公司 | Compressed air dehumidifying device |
| CN202792265U (en) * | 2012-09-12 | 2013-03-13 | 姜哲 | Air dehumidification gas-liquid separator |
| CN103933834A (en) * | 2013-01-17 | 2014-07-23 | 陈永真 | Whirlwind hot-air total heat recovery dedusting dehumidifying gas-water separator |
-
2015
- 2015-11-06 CN CN201510754804.5A patent/CN105251320A/en active Pending
Patent Citations (6)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| GB627838A (en) * | 1946-02-26 | 1949-08-17 | Sutcliffe Speakman And Company | Improvements relating to the continuous distillation of solvent or volatile liquids |
| CN2131594Y (en) * | 1992-07-20 | 1993-05-05 | 邓国桢 | Air drying machine |
| CN1715536A (en) * | 2004-07-02 | 2006-01-04 | 三星电子株式会社 | Cyclone type condenser and have the washing/drying machine of described condenser |
| CN202146635U (en) * | 2011-04-27 | 2012-02-22 | 安徽省皖北药业股份有限公司 | Compressed air dehumidifying device |
| CN202792265U (en) * | 2012-09-12 | 2013-03-13 | 姜哲 | Air dehumidification gas-liquid separator |
| CN103933834A (en) * | 2013-01-17 | 2014-07-23 | 陈永真 | Whirlwind hot-air total heat recovery dedusting dehumidifying gas-water separator |
Cited By (8)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN105768205A (en) * | 2016-05-11 | 2016-07-20 | 常德烟草机械有限责任公司 | Method and device for adjusting and controlling temperature of circulating air flow in fluidized bed |
| CN106178851A (en) * | 2016-08-15 | 2016-12-07 | 宁波德泰化学有限公司 | A kind of centrifugal classification dehydrating unit |
| CN106268200A (en) * | 2016-08-15 | 2017-01-04 | 宁波德泰化学有限公司 | A kind of classification dehydrating unit |
| CN106268200B (en) * | 2016-08-15 | 2019-08-13 | 宁波德泰化学有限公司 | A kind of classification dehumidification device |
| WO2019067849A1 (en) * | 2017-09-29 | 2019-04-04 | Bendix Commercial Vehicle Systems Llc | Effluent processing apparatus and method for a vehicle air brake charging system |
| US10583820B2 (en) | 2017-09-29 | 2020-03-10 | Bendix Commercial Vehicle Systems Llc | Effluent processing apparatus and method for a vehicle air brake charging system |
| CN111790240A (en) * | 2019-11-05 | 2020-10-20 | 山东建筑大学 | Multifunctional negative pressure type dehumidifying and heat exchanger |
| CN111841161A (en) * | 2020-07-29 | 2020-10-30 | 濮阳市盛源能源科技股份有限公司 | Gas-liquid separation device and pressure removal reaction kettle |
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Application publication date: 20160120 |