CN204563889U - Adsorption separation device - Google Patents
Adsorption separation device Download PDFInfo
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- CN204563889U CN204563889U CN201520145249.1U CN201520145249U CN204563889U CN 204563889 U CN204563889 U CN 204563889U CN 201520145249 U CN201520145249 U CN 201520145249U CN 204563889 U CN204563889 U CN 204563889U
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- adsorption
- separation device
- heat exchanger
- pipe group
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D53/00—Separation of gases or vapours; Recovering vapours of volatile solvents from gases; Chemical or biological purification of waste gases, e.g. engine exhaust gases, smoke, fumes, flue gases, aerosols
- B01D53/02—Separation of gases or vapours; Recovering vapours of volatile solvents from gases; Chemical or biological purification of waste gases, e.g. engine exhaust gases, smoke, fumes, flue gases, aerosols by adsorption, e.g. preparative gas chromatography
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D53/00—Separation of gases or vapours; Recovering vapours of volatile solvents from gases; Chemical or biological purification of waste gases, e.g. engine exhaust gases, smoke, fumes, flue gases, aerosols
- B01D53/26—Drying gases or vapours
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- Engineering & Computer Science (AREA)
- Analytical Chemistry (AREA)
- General Chemical & Material Sciences (AREA)
- Oil, Petroleum & Natural Gas (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Drying Of Gases (AREA)
Abstract
The utility model is applicable to adsorption separation device technical field, provide a kind of adsorption separation device, comprise adsorbing separation pipe group, air intake assembly and go out pneumatic module, air intake assembly has air inlet, go out pneumatic module and there is gas outlet, adsorption separation device also comprises temperature-adjusting device, and temperature-adjusting device comprises cold medium compressor, condenser, evaporimeter and heat exchanger, and cold medium compressor is connected with the refrigerant pipeline being arranged in condenser and heat exchanger.Adsorption separation device provided by the utility model, it, by set temperature adjusting device, enters adsorbing separation Guan Zuqian at gas, by evaporimeter, gas is lowered the temperature, to separate out portion of water, thus obtain better drying effect, and the heat produced during temperature-adjusting device work then can heat to regeneration air stream, to improve gas flow temperature, thus raising desorption ability, and then improving desorption performance, dry water removal effect is good, and plant energy consumption is low, product effects of energy conservation and environmental protection is good.
Description
Technical field
The utility model belongs to adsorption separation device technical field, particularly relates to a kind of adsorption separation device.
Background technology
Current adsorption separation device, it is generally only directly by adsorption separating agent dry gas, and dry water removal effect is not good enough.
Utility model content
The purpose of this utility model is to overcome above-mentioned the deficiencies in the prior art, provides a kind of adsorption separation device, the good and energy-conserving and environment-protective of its dry water removal effect.
The utility model is achieved in that a kind of adsorption separation device, comprise adsorbing separation pipe group, be connected to described adsorbing separation pipe group one end air intake assembly and be connected to the described adsorbing separation pipe group other end go out pneumatic module, described air intake assembly has the air inlet for flowing into for charge air flow, described go out pneumatic module have for confess entraining air stream flow out gas outlet, described adsorption separation device also comprises temperature-adjusting device, described temperature-adjusting device comprises cold medium compressor, condenser, for the evaporimeter of lowering the temperature to charge air flow and the heat exchanger for heating regeneration air stream, described cold medium compressor is connected with the refrigerant pipeline being arranged in described condenser and heat exchanger, refrigerant is provided with in described refrigerant pipeline.
Alternatively, described adsorbing separation pipe group comprises the many adsorption tubes longitudinally arranged, be provided with adsorption and separation material in described adsorption tube, described air intake assembly is connected to the below of described adsorbing separation pipe group, described in go out the top that pneumatic module is connected to described adsorbing separation pipe group.
Alternatively, described temperature-adjusting device is positioned at the side of described adsorbing separation pipe group, and wherein, described condenser is close to described air intake assembly, and described heat exchanger is positioned at the top of described condenser and goes out pneumatic module described in being close to.
Alternatively, described air intake assembly has buffering air inlet branch chamber, and described evaporimeter is arranged in described buffering air inlet branch chamber, and described evaporimeter is connected to described cold medium compressor by refrigerant pipeline.
Alternatively, described heat exchanger is provided with temp probe interface.
Alternatively, described adsorbing separation pipe group comprises first group of adsorbing separation pipe for hocket adsorbing separation and regeneration and second group of adsorbing separation pipe, described adsorbing separation pipe group is connected with the first regeneration control valve and the second regeneration control valve, described heat exchanger has regeneration air stream entrance and regeneration air stream outlet, described regeneration air stream entrance is connected to described first regeneration control valve, and described regeneration air stream outlet is connected to described second regeneration control valve.
Alternatively, described cold medium compressor has refrigerant inlet and refrigerant exit, and described heat exchanger has and connects into mouth and connection outlet; Described refrigerant inlet is connected with the first pipeline, described first pipeline is connected to described connection outlet through described condenser and heat exchanger successively from described refrigerant inlet, described refrigerant exit is connected with the second pipeline, and described second pipeline is connected to described connection entrance through described condenser and heat exchanger successively from described refrigerant exit.
Alternatively, described first pipeline is connected with refrigerant filter and expansion valve.
Alternatively, the side of described adsorbing separation pipe group is connected with the rotatable extension case opened, and described temperature-adjusting device is arranged in described extension case, and the arranged outside of described extension case has control panel.
Alternatively, the side of described condenser parts is connected with radiating subassembly, and described radiating subassembly comprises radiating motor and is connected to the flabellum of described radiating motor.
Adsorption separation device provided by the utility model, it is by set temperature adjusting device, adsorbing separation Guan Zuqian is entered at gas, by evaporimeter, gas is lowered the temperature, to separate out portion of water, thus obtain better drying effect, and the heat produced during temperature-adjusting device work then can heat regeneration air stream, to improve gas flow temperature, thus raising desorption ability, and then improving desorption performance, dry water removal effect is good, and plant energy consumption is low, product effects of energy conservation and environmental protection is good.
Accompanying drawing explanation
In order to be illustrated more clearly in the technical scheme in the embodiment of the present invention, be briefly described to the accompanying drawing used required in embodiment below, apparently, accompanying drawing in the following describes is only some embodiments of the present invention, for those of ordinary skill in the art, under the prerequisite not paying creative work, other accompanying drawing can also be obtained according to these accompanying drawings.
Fig. 1 is the front view of the adsorption separation device that the utility model embodiment provides;
Fig. 2 is the left view of the adsorption separation device that the utility model embodiment provides;
Fig. 3 hangs case to rotate schematic diagram when opening in the adsorption separation device that provides of the utility model embodiment;
Fig. 4 is the right view of the adsorption separation device that the utility model embodiment provides.
Detailed description of the invention
In order to make the purpose of this utility model, technical scheme and advantage clearly understand, below in conjunction with drawings and Examples, the utility model is further elaborated.Should be appreciated that specific embodiment described herein only in order to explain the utility model, and be not used in restriction the utility model.
It should be noted that, when element is called as " being fixed on " or " being arranged at " another element, it can directly on another element or may there is centering elements simultaneously.When an element is known as " being connected to " another element, it can be directly connected to another element or may there is centering elements simultaneously.
Also it should be noted that, the orientation term such as left and right, upper and lower in the utility model embodiment, is only relative concept or be reference with the normal operating condition of product each other, and should not be regarded as have restrictive.
As shown in Figure 1 to 4, a kind of adsorption separation device that the utility model embodiment provides, comprise adsorbing separation pipe group 3, be connected to described adsorbing separation pipe group 3 one end air intake assembly 1 and be connected to described adsorbing separation pipe group 3 other end go out pneumatic module 2, described air intake assembly 1 has the air inlet for flowing into for charge air flow, described go out pneumatic module 2 have for confess entraining air stream flow out gas outlet, described adsorption separation device also comprises temperature-adjusting device, described temperature-adjusting device comprises cold medium compressor 41, condenser 42, for the evaporimeter 43 of lowering the temperature to charge air flow and the heat exchanger 44 for heating regeneration air stream, described condenser 42 is connected with cold medium compressor 41, described cold medium compressor 41 is connected with the refrigerant pipeline being arranged in described condenser 42 and heat exchanger 44, refrigerant is provided with in described refrigerant pipeline.By set temperature adjusting device, before gas enters adsorbing separation pipe group 3, lower the temperature by evaporimeter 43 pairs of gases, to separate out portion of water, thus obtain better drying effect, and the heat produced during temperature-adjusting device work then can heat regeneration air stream, to improve gas flow temperature, thus improves desorption ability, and then improve desorption performance, dry water removal effect is good, and plant energy consumption is low, and product effects of energy conservation and environmental protection is good.
Particularly, described adsorbing separation pipe group 3 comprises the many adsorption tubes 31 longitudinally arranged, adsorption and separation material is provided with in described adsorption tube 31, described air intake assembly 1 is connected to the below of described adsorbing separation pipe group 3, described go out pneumatic module 2 be connected to the top of described adsorbing separation pipe group 3, adsorbing separation is effective.
Particularly, described temperature-adjusting device is positioned at the side of described adsorbing separation pipe group 3, wherein, described condenser 42 is close to described air intake assembly 1, described heat exchanger 44 is positioned at the top of described condenser 42 and goes out pneumatic module 2 described in being close to, it makes use of the principle of hot-air light specific gravity, improve the performance of equipment.
Particularly, described air intake assembly 1 has buffering air inlet branch chamber 101, and described evaporimeter 43 is arranged in described buffering air inlet branch chamber 101, and described evaporimeter 43 is connected to described cold medium compressor 41 by refrigerant pipeline.Evaporimeter 43 has multiple fin, and its surface area is large, good cooling results.Evaporimeter 43 can linearly shape or in roundabout tubulose etc., the such as suitable shape such as U-shaped or zigzag.
Particularly, described heat exchanger 44 is provided with temp probe interface 440, is conducive to the reliability improving product.
Particularly, described adsorbing separation pipe group 3 comprises first group of adsorbing separation pipe for hocket adsorbing separation and regeneration and second group of adsorbing separation pipe, described adsorbing separation pipe group 3 is connected with the first regeneration control valve 301 and the second regeneration control valve 302, by controlling adsorbing separation pipe group 3, while making first group of adsorbing separation pipe carry out adsorbing separation, second group of adsorbing separation pipe can carry out regeneration desorption, to export dry gas stream continually.
Particularly, described cold medium compressor 41 has refrigerant inlet 411 and refrigerant exit 412, and described heat exchanger 44 has connection entrance 441 and connection outlet 442; Described refrigerant inlet 411 is connected with the first pipeline 451, described first pipeline 451 is connected to described connection outlet 442 through described condenser 42 and heat exchanger 44 successively from described refrigerant inlet 411, described refrigerant exit 412 is connected with the second pipeline 452, described second pipeline 452 is connected to through described condenser 42 and heat exchanger 44 sequence of flow being refrigerant in described connection entrance 441, Fig. 3 shown in arrow successively from described refrigerant exit 412.Heat exchanger 44 has regeneration air stream entrance 444 and regeneration air stream outlet 443, and regeneration air stream entrance 444 is connected to the first regeneration control valve 301, and regeneration air stream outlet 443 is connected to the second regeneration control valve 302.
Particularly, described first pipeline 451 is connected with refrigerant filter 46 and expansion valve 47 (capillary).
Particularly, the side of described adsorbing separation pipe group 3 is connected with the rotatable extension case 48 opened, and described temperature-adjusting device is arranged in described extension case 48, and the arranged outside of described extension case 48 has control panel 49, so that operation and maintenance.Hang case 48 and multiple louvered shutter or louvre position are set.
Particularly, the side of described condenser 42 is connected with radiating subassembly, and described radiating subassembly comprises radiating motor and is connected to the flabellum of described radiating motor, its good heat dissipation effect.
Particularly, go out pneumatic module 2 and have voltage stabilizing air-flow and to conflux chamber 201, the side hanging case 48 is provided with power switch 481 (electrical control gear, electric control system).
Particularly, the bottom of air intake assembly 1 can be provided with muffler 12, and it is conducive to reducing noise, and result of use is good.
Adsorption separation device provided by the utility model, it is by set temperature adjusting device, before gas enters adsorbing separation pipe group 3, lower the temperature by evaporimeter 43 pairs of gases, to separate out portion of water, thus obtain better drying effect, and the heat produced during temperature-adjusting device work then can heat regeneration air stream, to improve gas flow temperature, thus raising desorption ability, and then improving desorption performance, dry water removal effect is good, and plant energy consumption is low, product effects of energy conservation and environmental protection is good.
The foregoing is only preferred embodiment of the present utility model; not in order to limit the utility model; all do within spirit of the present utility model and principle any amendment, equivalent to replace or improvement etc., all should be included within protection domain of the present utility model.
Claims (10)
1. an adsorption separation device, comprise adsorbing separation pipe group, be connected to described adsorbing separation pipe group one end air intake assembly and be connected to the described adsorbing separation pipe group other end go out pneumatic module, described air intake assembly has the air inlet for flowing into for charge air flow, described go out pneumatic module have for confess entraining air stream flow out gas outlet, it is characterized in that, described adsorption separation device also comprises temperature-adjusting device, described temperature-adjusting device comprises cold medium compressor, condenser, for the evaporimeter of lowering the temperature to charge air flow and the heat exchanger for heating regeneration air stream, described cold medium compressor is connected with the refrigerant pipeline being arranged in described condenser and heat exchanger, refrigerant is provided with in described refrigerant pipeline.
2. adsorption separation device as claimed in claim 1, it is characterized in that, described adsorbing separation pipe group comprises the many adsorption tubes longitudinally arranged, adsorption and separation material is provided with in described adsorption tube, described air intake assembly is connected to the below of described adsorbing separation pipe group, described in go out the top that pneumatic module is connected to described adsorbing separation pipe group.
3. adsorption separation device as claimed in claim 2, it is characterized in that, described temperature-adjusting device is positioned at the side of described adsorbing separation pipe group, wherein, described condenser is close to described air intake assembly, and described heat exchanger is positioned at the top of described condenser and goes out pneumatic module described in being close to.
4. adsorption separation device as claimed in claim 1, is characterized in that, described air intake assembly has buffering air inlet branch chamber, and described evaporimeter is arranged in described buffering air inlet branch chamber, and described evaporimeter is connected to described cold medium compressor by refrigerant pipeline.
5. adsorption separation device as claimed in claim 1, it is characterized in that, described heat exchanger is provided with temp probe interface.
6. adsorption separation device as claimed in claim 1, it is characterized in that, described adsorbing separation pipe group comprises first group of adsorbing separation pipe for hocket adsorbing separation and regeneration and second group of adsorbing separation pipe, described adsorbing separation pipe group is connected with the first regeneration control valve and the second regeneration control valve, described heat exchanger has regeneration air stream entrance and regeneration air stream outlet, described regeneration air stream entrance is connected to described first regeneration control valve, and described regeneration air stream outlet is connected to described second regeneration control valve.
7. the adsorption separation device according to any one of claim 1 to 6, is characterized in that, described cold medium compressor has refrigerant inlet and refrigerant exit, and described heat exchanger has and connects into mouth and connection outlet; Described refrigerant inlet is connected with the first pipeline, described first pipeline is connected to described connection outlet through described condenser and heat exchanger successively from described refrigerant inlet, described refrigerant exit is connected with the second pipeline, and described second pipeline is connected to described connection entrance through described condenser and heat exchanger successively from described refrigerant exit.
8. adsorption separation device as claimed in claim 7, it is characterized in that, described first pipeline is connected with refrigerant filter and expansion valve.
9. adsorption separation device as claimed in claim 7, is characterized in that, the side of described adsorbing separation pipe group is connected with the rotatable extension case opened, and described temperature-adjusting device is arranged in described extension case, and the arranged outside of described extension case has control panel.
10. the adsorption separation device according to any one of claim 1 to 6, is characterized in that, the side of described condenser parts is connected with radiating subassembly, and described radiating subassembly comprises radiating motor and is connected to the flabellum of described radiating motor.
Priority Applications (2)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201520145249.1U CN204563889U (en) | 2015-03-13 | 2015-03-13 | Adsorption separation device |
| PCT/CN2016/075467 WO2016145995A1 (en) | 2015-03-13 | 2016-03-03 | Adsorption-separation-apparatus |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201520145249.1U CN204563889U (en) | 2015-03-13 | 2015-03-13 | Adsorption separation device |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN204563889U true CN204563889U (en) | 2015-08-19 |
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Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201520145249.1U Active CN204563889U (en) | 2015-03-13 | 2015-03-13 | Adsorption separation device |
Country Status (2)
| Country | Link |
|---|---|
| CN (1) | CN204563889U (en) |
| WO (1) | WO2016145995A1 (en) |
Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| WO2016145995A1 (en) * | 2015-03-13 | 2016-09-22 | 深圳市贝腾科技有限公司 | Adsorption-separation-apparatus |
| CN109613146A (en) * | 2018-12-08 | 2019-04-12 | 苏州贞成分析仪器有限公司 | A kind of adsorption/desorption pipe |
| WO2022121209A1 (en) * | 2020-12-11 | 2022-06-16 | 深圳市贝腾科技有限公司 | Adsorptive separation apparatus |
Family Cites Families (7)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN1202896C (en) * | 2002-02-07 | 2005-05-25 | 北京燕化高新技术股份有限公司 | Air-purifying method during separating air |
| US9038409B2 (en) * | 2009-09-21 | 2015-05-26 | Korea Research Institute Of Chemical Technology | Apparatus for treating air by using porous organic-inorganic hybrid materials as an absorbent |
| CN202427328U (en) * | 2012-01-06 | 2012-09-12 | 郭应辉 | Absorption dryer |
| CN202460431U (en) * | 2012-01-06 | 2012-10-03 | 郭应辉 | Adsorption drying machine |
| CN102553403A (en) * | 2012-01-06 | 2012-07-11 | 郭应辉 | Adsorption drying machine |
| CN102553402A (en) * | 2012-01-06 | 2012-07-11 | 郭应辉 | Adsorption drying machine |
| CN204563889U (en) * | 2015-03-13 | 2015-08-19 | 郭应辉 | Adsorption separation device |
-
2015
- 2015-03-13 CN CN201520145249.1U patent/CN204563889U/en active Active
-
2016
- 2016-03-03 WO PCT/CN2016/075467 patent/WO2016145995A1/en active Application Filing
Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| WO2016145995A1 (en) * | 2015-03-13 | 2016-09-22 | 深圳市贝腾科技有限公司 | Adsorption-separation-apparatus |
| CN109613146A (en) * | 2018-12-08 | 2019-04-12 | 苏州贞成分析仪器有限公司 | A kind of adsorption/desorption pipe |
| WO2022121209A1 (en) * | 2020-12-11 | 2022-06-16 | 深圳市贝腾科技有限公司 | Adsorptive separation apparatus |
Also Published As
| Publication number | Publication date |
|---|---|
| WO2016145995A1 (en) | 2016-09-22 |
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Legal Events
| Date | Code | Title | Description |
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| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| C41 | Transfer of patent application or patent right or utility model | ||
| TR01 | Transfer of patent right |
Effective date of registration: 20161025 Address after: 518333, Guangdong, Shenzhen Xixiang street Baoan District iron road oyster industry park 1 and 2 buildings (first branch garden 1, workshop 4, C) Patentee after: Shenzhen Biteman Science & Technology Co.,Ltd. Address before: Shenzhen City, Guangdong province Baoan 518000 West Coast Garden District 48 Haifeng Ge 1-4C Patentee before: Guo Yinghui |