CN103894045A - High-humidity gas drying and separating device and method - Google Patents
High-humidity gas drying and separating device and method Download PDFInfo
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- CN103894045A CN103894045A CN201410159537.2A CN201410159537A CN103894045A CN 103894045 A CN103894045 A CN 103894045A CN 201410159537 A CN201410159537 A CN 201410159537A CN 103894045 A CN103894045 A CN 103894045A
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Abstract
The invention discloses a high-humidity gas drying and separating device. The high-humidity gas drying and separating device comprises an air intake pipe, a separating device and an air exhaust device, wherein the separating device is connected with the air intake pipe; the air exhaust device is connected with the separating device; the separating device comprises a condensation device and a liquid discharge device connected with the condensation device. The invention also discloses a high-humidity gas drying and separating method. A high-humidity gas is blown from an air inlet and bypasses the condensation device; moisture and particulate matter in the high-humidity gas are separated from the gas, and the separated gas is drawn out by the air exhaust device. According to the invention, the high-humidity gas enters the drying and separating device, the moisture and the particulate matter overwrapped in the moisture are dried and separated out by only utilizing the rapid temperature reduction of the condensation device; no drying adsorbent is required in the whole device, and the moisture and the particulate matter can be dried to the specified humidity range as required.
Description
Technical field
The present invention relates to a kind of gas Drying separator and method, specifically large humidity gas Drying separator and method.
Background technology
Current gas-drying apparatus general structure is complicated and use heat drier more, heat drier may cause unsettled gas formation to change or gas expansion exists potential safety hazard, be exactly the moisture using in regenerable sorbent adsorbed gas in addition, for example molecular sieve, discolour silica gel, anhydrous calcium chloride etc., if and the use under the environment of large humidity of these adsorbents just there will be a lot of drawbacks, easily cause absorbent powder, caking phenomenon, so just can not well be dried separation to gas, also can cause very large waste to the recycling of adsorbent simultaneously.
Summary of the invention
The object of the invention is the deficiency existing for prior art, a kind of large humidity gas Drying separator that meets working environment desired gas degree of drying that can simple and fast is provided.
For achieving the above object, the technical solution used in the present invention is a kind of large humidity gas Drying separator, the separator that comprises blast pipe, join with blast pipe and the exhaust apparatus joining with separator, the pumping equipment that described separator comprises condensing unit and joins with condensing unit.
For making separated from the gas more thorough of condensed liquid, described condensing unit is positioned at the top of blast pipe, and exhaust apparatus is positioned at the top of condensing unit, in the time that condensed fluid is enough large, because deadweight is fallen, be difficult for being affected drying effect by the wind of blast pipe to discharge pipe.
Described condensing unit comprises the condenser pipe that is connected with blast pipe, the refrigerant joining with condenser pipe and the compressor joining with refrigerant.
Described pumping equipment is arranged on condensing unit below, pumping equipment comprise be arranged in blast pipe and be positioned at the hydrops groove of condenser pipe below, the catheter joining with hydrops groove and the reservoir joining with catheter.
Described exhaust apparatus comprises the tail-end blower fan joining with condensing unit and the discharge pipe joining with tail-end blower fan.
Between described condensing unit and exhaust apparatus, be also provided with humidity measurement instrument, in humidity measurement instrument, be provided with the control device with condensing unit communication connection, control the working strength of condensing unit, control specifically working strength, the discharge rate of refrigerant and the working quantity of condenser pipe of compressor.
The invention also discloses a kind of dry method separating of large humidity gas, after large humidity gas is blown into by air inlet, through condensing unit, by separated from the gas to moisture, particulate material in large humidity gas, then by exhaust apparatus, the gas after separating is extracted out.
Described particulate material comprises dust, small mineral matter and/or harmful and noxious substance.
Described particulate material and moisture store by pumping equipment.
Large humidity gas described in the present invention, refer to water or containing surfactant or biology enzyme or delicate fragrance component or the disinfection component aqueous solution and airborne molecule as dust, poisonous and harmful substance, the well-mixed gas of small mineral matter.Large humidity gas enters after the condensing unit after compressor compresses refrigerant circulation, in large humidity gas, the moisture aggregation after device rapid cooling that is condensed becomes little water droplet, then aggregation is in hydrops groove, be directed in reservoir by catheter again, thereby by the moisture in large humidity gas and be wrapped in the many dust in moisture, small mineral matter and harmful and noxious substance particle separation out.
Beneficial effect: the present invention enters after Drying separator at large humidity gas, the rapid cooling that just utilizes condensing unit the moisture in large humidity gas and and be wrapped in dry the separating of particulate material in moisture, in whole device, do not need to use any dry adsorbent, and can be dried to as requested the humidity range of appointment.With respect to prior art, the present invention is simple in structure, very good to the dry separating effect of large humidity gas, and does not have the waste to adsorbent, has greatly saved resource.
Accompanying drawing explanation
Fig. 1 is structural representation of the present invention.
The specific embodiment
Below in conjunction with the drawings and specific embodiments, further illustrate the present invention, the present embodiment is implemented under take technical solution of the present invention as prerequisite, should understand these embodiment and only be not used in and limit the scope of the invention for the present invention is described.
As shown in Figure 1, a kind of large humidity gas Drying separator, the separator 2 that comprises blast pipe 1, join with blast pipe 1 and the exhaust apparatus 3 joining with separator 2, separator 2 comprises condensing unit 4 and pumping equipment 5, separator 2 is positioned at the top of blast pipe 1, and exhaust apparatus 3 is positioned at the top of separator 2.
Condensing unit 4 comprises the condenser pipe 6 that is connected with blast pipe 1, the refrigerant 7 joining with condenser pipe 6 and the compressor 8 joining with refrigerant 7.Pumping equipment 5 is connected to the below of condensing unit 4, and pumping equipment 5 comprises the catheter 10 that is arranged in blast pipe and be positioned at condenser pipe 6 belows hydrops groove 9, join with hydrops groove 9 and the reservoir 11 joining with catheter 10.Exhaust apparatus 3 comprises the tail-end blower fan 12 joining with condensing unit 4 and the discharge pipe 13 joining with tail-end blower fan 12.Between condensing unit 4 and exhaust apparatus 3, be also provided with humidity measurement instrument 14, in humidity measurement instrument 14, be provided with the control device communicating to connect with condensing unit 4, control the working strength of condensing unit 4.
When work, when the large humidity gas of environment is inhaled into from blast pipe 1, through by compressor 6 to the condenser pipe 4 of refrigerant 5 circulation compression refrigerations after, large humidity gas is by rapid cooling, moisture in large humidity gas is just condensed into little water droplet aggregation on condenser pipe 4 surfaces, in this process, the particulate material comprising in gas can be wrapped in water droplet, in the time that the little water droplet of aggregation is enough large, will drop onto in the hydrops groove 8 of condenser pipe 4 belows, hydrops groove 8 connects catheter 9, and liquid aggregation being got up by catheter 9 imports in reservoir 10, thereby by the moisture in large humidity gas and be wrapped in the many dust in moisture, small mineral matter and harmful and noxious substance particle separation are out.
Gas after super-dry separates is sent working environment back to by the extraction by force that is arranged on the tail-end blower fan 11 on discharge pipe 12, and by the humidity measurement instrument 13 being arranged on wind pipe, the gas being dried after separating is carried out to Humidity Detection, if gas degree of drying does not reach the requirement of expection, this dry separating cycle is proceeded to process; If gas degree of drying meets the requirement of expection, this dry separating cycle can temporarily stop processing.According to the different requirements of gas degree of drying, also can pass through control device, control working strength, the discharge rate of refrigerant and the working quantity of condenser pipe of compressor.
Claims (9)
1. a large humidity gas Drying separator, it is characterized in that: comprise blast pipe (1), the separator (2) joining with blast pipe (1) and the exhaust apparatus (3) joining with separator (2), the pumping equipment (5) that described separator (2) comprises condensing unit (4) and joins with condensing unit (4).
2. large humidity gas Drying separator according to claim 1, is characterized in that: described condensing unit (2) is positioned at the top of blast pipe (1), exhaust apparatus (3) is positioned at the top of condensing unit (2).
3. according to large humidity gas Drying separator described in claim 1 or 2, it is characterized in that: described condensing unit (4) comprises the condenser pipe (6) that is connected with blast pipe (1), the refrigerant (7) joining with condenser pipe (6) and the compressor (8) joining with refrigerant (7).
4. large humidity gas Drying separator according to claim 1, it is characterized in that: described pumping equipment (5) is arranged on condensing unit (4) below, pumping equipment (5) comprise be arranged in blast pipe and be positioned at the hydrops groove (9) of condenser pipe (6) below, the catheter (10) joining with hydrops groove (9) and the reservoir (11) joining with catheter (10).
5. large humidity gas Drying separator according to claim 1, is characterized in that: described exhaust apparatus (3) comprises the tail-end blower fan (12) joining with condensing unit (4) and the discharge pipe (13) joining with tail-end blower fan (12).
6. large humidity gas Drying separator according to claim 1, it is characterized in that: between described condensing unit (4) and exhaust apparatus (3), be also provided with humidity measurement instrument (14), in humidity measurement instrument (14), be provided with the control device communicating to connect with condensing unit (4), control the working strength of condensing unit (4).
7. the dry method separating of large humidity gas, is characterized in that: after large humidity gas is blown into by air inlet, through condensing unit, by separated from the gas to moisture, particulate material in large humidity gas, then by exhaust apparatus, the gas after separating is extracted out.
8. a kind of large humidity gas is dried the method separating according to claim 7, it is characterized in that: described particulate material comprises dust, small mineral matter and/or harmful and noxious substance.
9. according to the dry method separating of a kind of large humidity gas described in claim 7 or 8, it is characterized in that: described particulate material and moisture store by pumping equipment.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
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| CN201410159537.2A CN103894045A (en) | 2014-04-18 | 2014-04-18 | High-humidity gas drying and separating device and method |
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| Application Number | Priority Date | Filing Date | Title |
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| CN201410159537.2A CN103894045A (en) | 2014-04-18 | 2014-04-18 | High-humidity gas drying and separating device and method |
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| CN103894045A true CN103894045A (en) | 2014-07-02 |
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| CN201410159537.2A Pending CN103894045A (en) | 2014-04-18 | 2014-04-18 | High-humidity gas drying and separating device and method |
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Cited By (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN104117269A (en) * | 2014-07-27 | 2014-10-29 | 成都国光电子仪表有限责任公司 | Cylindrical natural gas drying device |
| CN104117268A (en) * | 2014-07-27 | 2014-10-29 | 成都国光电子仪表有限责任公司 | Network pipe type natural gas drying device |
| CN107349719A (en) * | 2017-08-31 | 2017-11-17 | 江苏天琦生物科技有限公司 | A kind of polypeptide airflow filtering drying device |
| CN113457327A (en) * | 2021-08-03 | 2021-10-01 | 贵州泓林机械科技有限公司 | A scrubbing tower for gaseous dust fall |
| CN115957582A (en) * | 2023-03-17 | 2023-04-14 | 长安大学 | Air adsorption and filtration device for road dust removal |
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| CN201470298U (en) * | 2009-08-11 | 2010-05-19 | 张文波 | Dryer |
| CN203155062U (en) * | 2013-04-16 | 2013-08-28 | 庄件付 | Gas drying and temperature-regulating device |
| CN203494377U (en) * | 2013-10-16 | 2014-03-26 | 上海石大机电有限公司 | Voltage-stabilization split type freezer dryer |
| CN203853001U (en) * | 2014-04-18 | 2014-10-01 | 德合南京智能技术有限公司 | High-humidity gas drying and separating device |
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2014
- 2014-04-18 CN CN201410159537.2A patent/CN103894045A/en active Pending
Patent Citations (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN201470298U (en) * | 2009-08-11 | 2010-05-19 | 张文波 | Dryer |
| CN203155062U (en) * | 2013-04-16 | 2013-08-28 | 庄件付 | Gas drying and temperature-regulating device |
| CN203494377U (en) * | 2013-10-16 | 2014-03-26 | 上海石大机电有限公司 | Voltage-stabilization split type freezer dryer |
| CN203853001U (en) * | 2014-04-18 | 2014-10-01 | 德合南京智能技术有限公司 | High-humidity gas drying and separating device |
Cited By (7)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN104117269A (en) * | 2014-07-27 | 2014-10-29 | 成都国光电子仪表有限责任公司 | Cylindrical natural gas drying device |
| CN104117268A (en) * | 2014-07-27 | 2014-10-29 | 成都国光电子仪表有限责任公司 | Network pipe type natural gas drying device |
| CN104117269B (en) * | 2014-07-27 | 2016-05-11 | 成都国光电子仪表有限责任公司 | Cartridge type natural gas drying device |
| CN104117268B (en) * | 2014-07-27 | 2016-08-24 | 成都国光电子仪表有限责任公司 | Network pipe type natural gas drying device |
| CN107349719A (en) * | 2017-08-31 | 2017-11-17 | 江苏天琦生物科技有限公司 | A kind of polypeptide airflow filtering drying device |
| CN113457327A (en) * | 2021-08-03 | 2021-10-01 | 贵州泓林机械科技有限公司 | A scrubbing tower for gaseous dust fall |
| CN115957582A (en) * | 2023-03-17 | 2023-04-14 | 长安大学 | Air adsorption and filtration device for road dust removal |
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Application publication date: 20140702 |