CN103239943B - Solid-containing vapor-state substance separation device - Google Patents
Solid-containing vapor-state substance separation device Download PDFInfo
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- CN103239943B CN103239943B CN201310175853.4A CN201310175853A CN103239943B CN 103239943 B CN103239943 B CN 103239943B CN 201310175853 A CN201310175853 A CN 201310175853A CN 103239943 B CN103239943 B CN 103239943B
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Abstract
The invention discloses a solid-containing vapor-state substance separation device, which comprises a machine body with a feeding port, wherein at least two space areas for separating solid-containing vapor-state substances are arranged in the machine body, and the space areas comprise a settling area for settling solid particles and a condensation area which is communicated with the settling area and is used for separating the remaining substances after the settling area is treated; the separation device is respectively discharged after being correspondingly separated into three forms of solid, gas and liquid according to the product form. The separation device of the invention utilizes the inherent characteristics of solid and vapor substances to separate, and a settling zone and a condensing zone are designed to separate the solid and vapor substances. The separation device can greatly reduce energy consumption, reduce the generation of sewage, eliminate the consumption of water resources, realize energy conservation and emission reduction and greatly reduce the operation cost.
Description
Technical field
The present invention relates to the separator of the applications such as a kind of industrial circle, sphere of life, particularly relate to after a kind of being applicable to organic matter, living beings, being decomposed to form solid, steam state thing containing organic matter biomass mixture and part inorganic matter, utilize these solids, the inherent characteristic of steam state thing carries out the separator that is separated.
Background technology
Along with the development of China's economy, industrial production obtains extensive development, but industrial production brings the industrial refuses such as a large amount of air-borne dust pollutions and sewage, and in addition, city domestic sewage and dust etc. are also significantly rise in discharge capacity in recent years.At present, the world and Environmental Protection in China technology are also along with the development of filtering technique is in continuous raising, filter from the thick effect of initial cloth bag, filter screen, to gravity scrubbing, cloth bag scrubbing, electrostatic scrubbing, filter vat scrubbing made of paper, sintered plate scrubbing etc. now, but the scavenging effect of these trash-removal devices or method is not good, fail to solve well the pollution problem of dust, waste gas and sewage.
At present, at chemical industry, iron and steel, the industries such as electric power all can produce a large amount of moisture vapors, the sewage of waste gas and dust is directly discharged in environment, in addition, dry materials is also present in industrial production and farming and animal husbandry processing in a large number, in existing dry materials technique, also directly discharge after all the waste gas produced being processed a little all in environment, the waste gas containing a large amount of water vapour produced in these industrial and agricultural productions is often directly discharge after mixing with sewage, not only can cause heat to environment, the pollutions such as dust, also can the reproducible heat energy of large losses in vain, significantly add production cost.
For dry materials process disposal system, the waste gas produced in dry materials, mainly based on saturated vapor, contains a small amount of dust and various on-condensible gas in waste gas.In traditional handicraft, waste gas directly discharges or discharge waits measure after cooling, and these measures not only to environment, and need the huge cooling device of construction for processing waste gas, consumes a large amount of electric energy and cooling water to maintain operation.For municipal sludge drying system, the wet mud of the every dry 1 ton of moisture content 80% of existing drying machine needs the saturated vapor about 0.9 ton of 0.5MPa, produce the saturated exhaust steam about 0.75 ton under normal pressure, purified treatment through special process flow process is good, and the superheated steam of the 0.25 ton 1MPa250 DEG C saturated clean steam promoted under 0.65 ton of normal pressure can be utilized can to obtain the saturated vapor of 0.9 ton of 0.5MPa.Consider the saturated vapor of the convertible 1.07 tons of 0.5MPa of the superheated steam of 1 ton MPa250 DEG C, after systemic circulation utilizes exhaust steam, comparable original system reduces steam consumption 70%, and the wet mud of every dry 1 ton of moisture content 80% can save cooling water about 15 tons.
Up to now, China does not also have the mature technology of a set of dust-laden exhaust steam energy recovery, needs a large amount of low-temperature heat source to carry out drying to wet stock especially, produce again in the system of a large amount of exhaust steam subsequently at drying sludge etc., now all adopts condensation process.Waste a large amount of condensed water resources, produce a large amount of condensation sewage, the steam of at substantial, operating cost remains high.
Summary of the invention
Technical problem to be solved by this invention is the defect overcoming prior art, there is provided a kind of dedusting, clean gas, purifying water effect quite high containing solid steam state thing separator, this separator is applicable to organic matter, living beings, is decomposed to form solid, steam state thing containing organic matter biomass mixture and part inorganic matter, utilize these solids, the inherent characteristic of steam state thing is separated, be separated into solid-state, gaseous state and liquid three kinds of form materials.
The technical solution adopted for the present invention to solve the technical problems is: a kind of containing solid steam state thing separator, comprise the body containing feeding mouth, be provided with in described body and be separated containing at least two area of space of solid steam state thing, be included in be provided with settle solids particle in described body decanting zone, steam state material with decanting zone conducting and after processing for separating of decanting zone condensing zone.Separator is discharged after being correspondingly separated into solid-state, gaseous state and liquid three kinds of form materials according to product form separately.Separator of the present invention utilizes solid, the inherent characteristic of steam state thing is separated, and design decanting zone is separated solid with condenser with steam state thing.
Further, described condensing zone is provided with condensation entrance and is connected conducting with decanting zone, and condensing zone is also provided with liquid outlet, and condensation entrance height, higher than liquid outlet height, is provided with the gas outlet higher than condensation entrance and liquid outlet in condensing zone.Further, include hydrops district in described condensing zone, by condensate outlet conducting between condensing zone and hydrops district, liquid outlet is located at hydrops district, and condensate outlet height is lower than liquid outlet height.Enter from feeding mouth containing solid-state steam state thing, first through decanting zone solid sedimentation separation, steam state thing after process enters condensing zone, in condensing zone, liquid outlet can be closed or be provided with certain liquid object in advance, liquid object height is higher than condensate outlet, when the steam state thing after solid enters condensing zone, after condensation, liquid object can accumulate in hydrops district, when liquid level is higher than condensate outlet, just can open liquid outlet, gaseous state thing is then discharged due to the characteristic of self from the gas outlet of condensing zone or recycles, and liquid object is then discharged by liquid outlet.And condensation entrance height is higher and lower than condensation entrance than condensate outlet higher than condensate outlet height, liquid outlet, the design of the height of these entry/exit mouths is inherent characteristic according to solid and steam state thing and arranges.
Further, described bottom, decanting zone is provided with and pushes the pressing device that solid sediment discharges decanting zone.The power set that described pressing device is included in decanting zone outer setting and the screw feeder driven by power set in decanting zone inner bottom part.Pressing device also can be screw feeder push type and the mode such as screw propelling, piston-propelled.Screw feeder can be delivered to the solids fallen to bottom decanting zone the front of screw feeder, so that the smooth discharge of solids.And the adoptable motor of power set.
Further, be extended with the elongated area be positioned at below condensing zone and hydrops district bottom described decanting zone, screw feeder is located in decanting zone and elongated area, and the discharge end of elongated area is connected with the discharge nozzle be upturned, and discharge nozzle is provided with discharge gate.Screw feeder pushes the solids in decanting zone into elongated area, and enters discharge nozzle from elongated area, discharges from discharge gate.
Further, described discharge gate inner bottom part is higher than elongated area discharge end inwall peak.
Further, described discharge nozzle is also provided with the seal of the sealing discharging mouth when first use separator.During first use separator, the seal is sealing discharging mouth, after use separator a period of time, when settle solids thing can block discharge gate, the seal can be extracted out or open, realize solia particle and discharge from discharge gate.The seal can be and is wound around filler, weaving filler, shaping filler or seal cover etc.
Further, the dividing plate stopping and contain solid steam state thing flow path every stream effect and prolongation is provided with.Dividing plate can improve the settling efficiency of decanting zone, containing solid steam state thing enter decanting zone entered dividing plate time, dividing plate reduces the flow velocity containing solid steam state thing, extends the flow path containing solid steam state thing, makes solid particle fully be settled down to the bottom of decanting zone gradually along dividing plate.
Further, also condensate film is provided with in described condensing zone.Condensate film can improve the condensation effect of condensing zone, plays the effect of assisted Extraction high effect.
In sum, of the present invention containing solid steam state thing separator, utilize solid, the inherent characteristic of steam state thing is separated, design decanting zone is separated solid with condensing zone with steam state thing.And the condensation entrance height of this separator, condensate outlet height, liquid outlet height, discharge nozzle height and discharge nozzle caliber are all particular design could realize function and the effect of this separator.This separator significantly can reduce energy consumption, reduces the generation of sewage, eliminates the consumption of water resource, realizes energy-saving and emission-reduction and significantly lower operating cost.
Accompanying drawing explanation
Fig. 1 is the structural representation containing solid steam state thing separator of the embodiment of the present invention 1;
Fig. 2 is the top view of Fig. 1;
Fig. 3 is the structural representation containing solid steam state thing separator of the embodiment of the present invention 3;
Fig. 4 is the structural representation containing solid steam state thing separator of the embodiment of the present invention 4;
Fig. 5 is the structural representation containing solid steam state thing separator of the embodiment of the present invention 5.
Detailed description of the invention
Embodiment 1
One described by the embodiment of the present invention 1, containing solid steam state thing separator, as shown in Figure 1 and Figure 2, comprises the body 2 containing feeding mouth 1.Be provided with in described body be separated containing solid steam state thing become gaseous state, liquid state and solid states three area of space, these three area of space are the decanting zone 3 of settle solids particle, the condensing zone 4 of the remaining material with decanting zone conducting and after processing for separating of decanting zone, the hydrops district 5 that is connected with condensing zone conducting.Body is welded into an entirety with metallic plate cutting on jagged metal tube, and the notch length of metal tube equals the length of decanting zone.
Further, condensing zone top is provided with condensation entrance 6 and is connected conducting with decanting zone, and condensing zone bottom is provided with condensate outlet 7, and condensing zone and hydrops district are by condensate outlet conducting; Condensation entrance height is higher than condensate outlet height, and condensing zone top is provided with gas outlet 8, and hydrops district is provided with higher than condensate outlet, lower than condensation entrance liquid outlet 9, and namely condensation entrance height is higher than liquid outlet height, and liquid outlet height is higher than condensate outlet height.Enter from feeding mouth containing solid-state steam state thing, first through decanting zone solid sedimentation separation, steam state thing after process enters condensing zone, in condensing zone, liquid outlet can be closed or be provided with certain liquid object in advance, liquid object height is higher than condensate outlet, when the steam state thing after solid enters condensing zone, after condensation, liquid object can accumulate in hydrops district, when liquid level is higher than condensate outlet, just can open liquid outlet, gaseous state thing is then discharged due to the characteristic of self from the gas outlet of condensing zone or recycles, and liquid object is then discharged by liquid outlet.And condensation entrance height is higher and lower than condensation entrance than condensate outlet higher than condensate outlet height, liquid outlet, the design of the height of these entry/exit mouths is inherent characteristic according to solid and steam state thing and arranges.
Further, described bottom, decanting zone is provided with the pressing device pushing solid sediment.The power set that described pressing device is included in decanting zone outer setting and the screw feeder 12 driven by power set bottom decanting zone.Power set are the motor 10 be located on body, reduction 11, reduction and screw feeder connection for transmission.Motor is buncher, according to settle solids thing number select be applicable to export speed.
Further, be extended with the elongated area 13 be positioned at below condensing zone and hydrops district bottom described decanting zone, screw feeder is located in decanting zone and elongated area, and the discharge end of elongated area is connected with the discharge nozzle 14 be upturned, and discharge nozzle is provided with discharge gate 15.Screw feeder pushes the solids in decanting zone into elongated area, and enters discharge nozzle from elongated area, discharges from discharge gate.
Further, discharge gate inner bottom part is higher than elongated area discharge end inwall peak.
Further, described discharge nozzle is also provided with the seal 16 of the sealing discharging mouth when first use separator.During first use separator, the seal is sealing discharging mouth, after use separator a period of time, the seal can be extracted out or open, realize solia particle and discharge from discharge gate.The seal can be and is wound around filler, weaving filler, shaping filler or seal cover etc.
Embodiment 2
The present embodiment changes on the basis of embodiment 1, specific as follows: as shown in Figure 3, the difference containing solid steam state thing separator and embodiment 1 of the present embodiment is two area of space being provided with the different shape such as separating solids and steam state in body, these two area of space are decanting zone 3 and condensing zone 4, after the steam state thing entering condensing zone from decanting zone is separated into gas and steam, gas is discharged from gas outlet, steam to be melted in condensing zone liquid and to discharge condensing zone, liquid outlet is located at condensing zone, and condensing zone eliminates condensate outlet.
Embodiment 3
The present embodiment is change on the basis of embodiment 1 equally, as shown in Figure 4, the present embodiment is same with the body of embodiment 2 is be provided with decanting zone 3 and these two area of space of condensing zone 4, but with the difference of embodiment 2, embodiment 3 is that embodiment 3 eliminates the setting of discharge nozzle, the solid particle after sedimentation is directly discharged from elongated area by the conveying of screw feeder.Liquid outlet is also located at condensing zone, and condensing zone eliminates condensate outlet.
Embodiment 4
The present embodiment is change on the basis of embodiment 1 equally, as shown in Figure 5, this embodiment 4 and the difference of embodiment 1 are that the present embodiment 4 has additional in decanting zone and stop every stream effect and extend the dividing plate 17 that contains solid steam state thing flow path and in condensing zone, have additional condensate film 18, this dividing plate is provided with polylith, dividing plate is for be vertically arranged in decanting zone, according to hydromechanical principle, be parallel longitudinal setting between every block dividing plate and there is between adjacent separator certain difference in height; This condensate film is also vertical setting.Dividing plate and condensate film not only can vertically be arranged, also can horizontally set.
The above is only preferred embodiment of the present invention, not does any pro forma restriction to technology contents of the present invention.Every above embodiment is done according to technical spirit of the present invention any simple modification, equivalent variations and modification, all still belong in the scope of technical scheme of the present invention.
Claims (9)
1. one kind contains solid steam state thing separator, comprise the body containing feeding mouth, it is characterized in that: be provided with in described body and be separated containing at least two area of space of solid steam state thing, be included in be provided with settle solids particle in described body decanting zone, steam state material with decanting zone conducting and after processing for separating of decanting zone condensing zone; Separator is discharged after being correspondingly separated into solid-state, gaseous state and liquid three kinds of form materials according to product form separately; Described condensing zone is provided with condensation entrance and is connected conducting with decanting zone, and condensing zone is also provided with liquid outlet, and condensation entrance height, higher than liquid outlet height, is provided with the gas outlet higher than condensation entrance and liquid outlet in condensing zone.
2. one according to claim 1 is containing solid steam state thing separator, it is characterized in that: in described condensing zone, include hydrops district, by condensate outlet conducting between condensing zone and hydrops district, liquid outlet is located at hydrops district, and condensate outlet height is lower than liquid outlet height.
3. the one according to claim 1-2 any one, containing solid steam state thing separator, is characterized in that: described bottom, decanting zone is provided with and pushes the pressing device that solid sediment discharges decanting zone.
4. one according to claim 3 is containing solid steam state thing separator, it is characterized in that: the power set that described pressing device is included in decanting zone outer setting and the screw feeder driven by power set in decanting zone inner bottom part.
5. one according to claim 4 is containing solid steam state thing separator, it is characterized in that: bottom described decanting zone, be extended with the elongated area be positioned at below condensing zone and hydrops district, screw feeder is located in decanting zone and elongated area, the discharge end of elongated area is connected with the discharge nozzle be upturned, and the end of discharge nozzle is discharge gate.
6. one according to claim 5 is containing solid steam state thing separator, it is characterized in that: described discharge gate inner bottom part is higher than elongated area discharge end inwall peak.
7. one according to claim 5 is containing solid steam state thing separator, it is characterized in that: described discharge nozzle is also provided with the seal of the sealing discharging mouth when first use separator.
8. one according to claim 1 is containing solid steam state thing separator, it is characterized in that: be also provided with in described decanting zone and stop every stream effect and extend the dividing plate containing solid steam state thing flow path.
9. one according to claim 1 is containing solid steam state thing separator, it is characterized in that: be also provided with condensate film in described condensing zone.
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| Application Number | Priority Date | Filing Date | Title |
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| CN201310175853.4A CN103239943B (en) | 2013-05-14 | 2013-05-14 | Solid-containing vapor-state substance separation device |
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| CN201310175853.4A CN103239943B (en) | 2013-05-14 | 2013-05-14 | Solid-containing vapor-state substance separation device |
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| CN103239943A CN103239943A (en) | 2013-08-14 |
| CN103239943B true CN103239943B (en) | 2015-09-23 |
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| CN114225565A (en) * | 2021-12-21 | 2022-03-25 | 中国科学院上海应用物理研究所 | Fluorine-containing gas buffer tank |
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| EP0476449A2 (en) * | 1990-09-19 | 1992-03-25 | Beb Erdgas Und Erdöl Gmbh | Method and apparatus for drying natural gas and for the recycling of the water solvent used for this |
| CN101053701A (en) * | 2007-05-18 | 2007-10-17 | 中南大学 | Device for chemical gaseous phase deposition industrial furnace tail gas purification |
| CN201832491U (en) * | 2010-09-30 | 2011-05-18 | 赵旭荣 | Separation device for dusty gas generated by pyrogenation of organic waste |
| JP4938536B2 (en) * | 2007-04-13 | 2012-05-23 | シャープ株式会社 | Air conditioner |
| CN202376791U (en) * | 2011-12-18 | 2012-08-15 | 山东福洋生物科技有限公司 | Dried exhaust discharging and precipitating device |
| CN202516420U (en) * | 2012-03-13 | 2012-11-07 | 上海金匙环保科技股份有限公司 | Oil-gas purifying device |
| CN203315878U (en) * | 2013-05-14 | 2013-12-04 | 陈朝阳 | Solid-containing vaporized material separation device |
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2013
- 2013-05-14 CN CN201310175853.4A patent/CN103239943B/en active Active
Patent Citations (7)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| EP0476449A2 (en) * | 1990-09-19 | 1992-03-25 | Beb Erdgas Und Erdöl Gmbh | Method and apparatus for drying natural gas and for the recycling of the water solvent used for this |
| JP4938536B2 (en) * | 2007-04-13 | 2012-05-23 | シャープ株式会社 | Air conditioner |
| CN101053701A (en) * | 2007-05-18 | 2007-10-17 | 中南大学 | Device for chemical gaseous phase deposition industrial furnace tail gas purification |
| CN201832491U (en) * | 2010-09-30 | 2011-05-18 | 赵旭荣 | Separation device for dusty gas generated by pyrogenation of organic waste |
| CN202376791U (en) * | 2011-12-18 | 2012-08-15 | 山东福洋生物科技有限公司 | Dried exhaust discharging and precipitating device |
| CN202516420U (en) * | 2012-03-13 | 2012-11-07 | 上海金匙环保科技股份有限公司 | Oil-gas purifying device |
| CN203315878U (en) * | 2013-05-14 | 2013-12-04 | 陈朝阳 | Solid-containing vaporized material separation device |
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Effective date of registration: 20180802 Address after: 529200 No. 12, North Keng Industrial Zone, Taicheng, Taishan, Guangdong. Patentee after: Taishan Volkswagen Environmental Protection Technology Co., Ltd. Address before: 529000 toad head hill, stone village, Tangxia Town, Pengjiang District, Jiangmen, Guangdong, China Co-patentee before: Tan Guangyi Patentee before: Chen Chaoyang Co-patentee before: Huang Xihong |
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Address after: 529200 Building 1, No. 12, Taicheng Beikeng Industrial Zone, Taishan City, Jiangmen City, Guangdong Province Patentee after: Taishan Volkswagen Environmental Protection Technology Co.,Ltd. Address before: 529200 No. 12, North Keng Industrial Zone, Taicheng, Taishan, Guangdong. Patentee before: Taishan Volkswagen Environmental Protection Technology Co.,Ltd. |
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