CN203315878U - Solid-containing vaporized material separation device - Google Patents
Solid-containing vaporized material separation device Download PDFInfo
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- CN203315878U CN203315878U CN2013202581077U CN201320258107U CN203315878U CN 203315878 U CN203315878 U CN 203315878U CN 2013202581077 U CN2013202581077 U CN 2013202581077U CN 201320258107 U CN201320258107 U CN 201320258107U CN 203315878 U CN203315878 U CN 203315878U
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- steam state
- zone
- state thing
- containing solid
- decanting zone
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Abstract
The utility model discloses a solid-containing vaporized material separation device which comprises a machine body, wherein the machine body comprises a feed port, and the machine body is internally provided with at least two space regions which separate solid-containing vaporized materials; the space regions include a subsiding region provided with subsiding solid granules in the machine body and a condensing region communicated with the subsiding region and used for separating substances remained after being treated in the subsiding region; the separation device correspondingly separates a product into three-state substances, namely solid substances, vaporized substances and liquid substances, and then respectively discharges. The solid-containing vaporized material separation device disclosed by the utility model carries out separation by utilizing the inherent characteristics of solids and the vaporized materials, can be used for separating the solids and the vaporized materials by designing the subsiding region and the condensing region and can greatly reduce the energy consumption, reduce the generation of sewage, eliminate the consumption of resources, realize the energy conservation and emission reduction and greatly reduce the operating cost.
Description
Technical field
The utility model relates to the separator of the applications such as a kind of industrial circle, sphere of life, after relating in particular to a kind of applicable organic matter, living beings, containing organic matter biomass mixture and part inorganic matter, being decomposed to form solid, steam state thing, the separator that utilizes the inherent characteristic of these solids, steam state thing to be separated.
Background technology
Along with the development of China's economy, industrial production has obtained extensive development, but industrial production is brought the industrial refuses such as a large amount of air-borne dust pollutions and sewage, and in addition, city domestic sewage and dust etc. also are significantly rising in discharge capacity in recent years.At present, international and Environmental Protection in China technology also along with the development of filtering technique in continuous raising, from the thick effect of initial cloth bag, filter screen, filter, to gravity scrubbing now, cloth bag scrubbing, static scrubbing, filter vat scrubbing made of paper, sintered plate scrubbing etc., but the scrubbing poor effect of these trash-removal devices or method, 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 directly is discharged in environment, in addition, dry materials also is present in industrial production and farming and animal husbandry processing in a large number, in existing dry materials technique, after also all the waste gas produced being processed a little, directly discharge all in environment, the waste gas that contains a large amount of water vapours 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 lose in vain a large amount of reproducible heat energy, significantly increased production cost.
It is example that the dry materials of take is processed disposal system, and the waste gas produced in dry materials mainly be take saturated vapor as main, contains a small amount of dust and various on-condensible gas in waste gas.At waste gas in traditional handicraft, directly discharge or the measure such as discharge after cooling, these measures are not only to environment, and need to build huge cooling device for processing waste gas, consume a large amount of electric energy and cooling water and maintain operation.Take the municipal sludge drying system as example, the wet mud of the existing every dry 1 ton of moisture content 80% of drying machine needs 0.9 ton of left and right of saturated vapor of 0.5MPa, produce the 0.75 ton of left and right of saturated exhaust steam under normal pressure, purified treatment through the special process flow process is good, can utilize the superheated steam of 0.25 ton 1MPa250 ℃ to promote the saturated vapor that saturated clean steam under 0.65 ton of normal pressure can obtain 0.9 ton of 0.5MPa.Consider the saturated vapor of the convertible 1.07 tons of 0.5MPa of superheated steam of 1 ton MPa250 ℃, after systemic circulation is utilized exhaust steam, comparable original system reduces steam consumption 70%, and the wet mud of every dry 1 ton of moisture content 80% can be saved 15 tons of left and right of cooling water.
Up to now, China does not also have the mature technology of a set of dust-laden exhaust steam energy recovery, at a large amount of low-temperature heat sources of the needs such as drying sludge, wet stock is carried out to drying especially, produces again subsequently in the system of a large amount of exhaust steam, the existing condensation process that all adopts.Wasted a large amount of condensed water resources, produced a large amount of condensation sewage, expended a large amount of steam, operating cost is high.
Summary of the invention
Technical problem to be solved in the utility model is the defect that overcomes prior art, provide 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, containing organic matter biomass mixture and part inorganic matter, is decomposed to form solid, steam state thing, utilize the inherent characteristic of these solids, steam state thing to be separated, be separated into solid-state, gaseous state and liquid three kinds of form materials.
The utility model solves the technical scheme that its technical problem adopts: a kind of containing solid steam state thing separator, comprise the body that contains feeding mouth, be provided with at least two area of space that separate containing solid steam state thing in described body, be included in the decanting zone ,Yu decanting zone conducting that is provided with the settle solids particle in described body and for separating of decanting zone, process after the condensing zone of steam state material.Separator is discharged after correspondingly being separated into solid-state, gaseous state and liquid three kinds of form materials according to the product form separately.Separator of the present utility model utilizes the inherent characteristic of solid, steam state thing to be separated, and separate solid with condenser the design decanting zone with the steam state thing.
Further, described condensing zone is provided with the condensation entrance and is connected conducting with decanting zone, and condensing zone also is provided with liquid outlet, and the condensation entrance height, higher than the liquid outlet height, is provided with the gas outlet higher than condensation entrance and liquid outlet in condensing zone.Further, include the hydrops district in described condensing zone, between condensing zone and hydrops district, by condensation, export conducting, liquid outlet is located at the hydrops district, and condensation goes out open height lower than the liquid outlet height.Containing solid-state steam state thing, from feeding mouth, enter, at first through decanting zone the solid sedimentation separation, steam state thing after processing enters condensing zone, in condensing zone, can close liquid outlet or be provided with in advance certain liquid object, the liquid object height exports higher than condensation, when the steam state thing except after solid enters condensing zone, after condensation, liquid object can accumulate in the hydrops district, when liquid level exports higher than condensation, just can open liquid outlet, the gaseous state thing is discharged or recycles from the gas outlet of condensing zone due to the characteristic of self, and liquid object is discharged by liquid outlet.And that the condensation entrance height goes out open height, liquid outlet higher than condensation is higher and lower than condensation entrance than the condensation outlet, these height designs that enter/export are to arrange according to the inherent characteristic of solid and steam state thing.
Further, bottom, described decanting zone is provided with and pushes the pressing device that the solid precipitum is discharged decanting zone.Described pressing device is included in the power set of decanting zone outer setting and the screw feeder driven by power set in the decanting zone inner bottom part.Pressing device can be also the modes such as screw feeder push type and screw propelling, piston-propelled.Screw feeder can be delivered to the solids that falls to the bottom, decanting zone in the place ahead of screw feeder, so that the smooth discharge of solids.And the adoptable motor of power set.
Further, bottom, described decanting zone is extended with the elongated area that is positioned at condensing zone and below, hydrops district, and the discharge end that screw feeder is located at decanting zone and Nei， elongated area, 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 ，Bing Cong elongated area, elongated area and enters discharge nozzle, from discharge gate, discharges.
Further, described discharge gate inner bottom part is higher than elongated area discharge end inwall peak.
Further, described discharge nozzle also is provided with the seal of sealing discharging mouth when first use separator.First while using separator, the seal is the sealing discharging mouth, using separator after a period of time, when the settle solids thing can be blocked discharge gate, can extract the seal or open out, realizes that solia particle discharges from discharge gate.The seal can be and is wound around filler, weaving filler, moulding filler or seal cover etc.
Further, be provided with and stop every the stream effect and extend the dividing plate containing the moving distance of solid steam state logistics.Dividing plate can improve the settling efficiency of decanting zone, when containing solid steam state thing, entering decanting zone and advanced dividing plate, dividing plate reduces the flow velocity containing solid steam state thing, extends the flow path containing solid steam state thing, makes solid particle fully along dividing plate, be settled down to gradually the bottom of decanting zone.
Further, also be provided with condensate film in described condensing zone.Condensate film can improve the condensation effect of condensing zone, plays the effect of the high effect of assisted Extraction.
In sum, the solid steam state thing separator that contains of the present utility model, utilize the inherent characteristic of solid, steam state thing to be separated, and separate solid with condensing zone the design decanting zone with the steam state thing.And condensation entrance height, the condensation of this separator go out open height, liquid outlet height, discharge nozzle height and discharge nozzle caliber, be all that particular design could realize function and the effect that this separates device.This separator can significantly reduce energy consumption, reduces the generation of sewage, eliminates the consumption of water resource, realizes energy-saving and emission-reduction and significantly lowers operating cost.
The accompanying drawing explanation
Fig. 1 is the structural representation containing solid steam state thing separator of the utility model embodiment 1;
Fig. 2 is the top view of Fig. 1;
Fig. 3 is the structural representation containing solid steam state thing separator of the utility model embodiment 3;
Fig. 4 is the structural representation containing solid steam state thing separator of the utility model embodiment 4;
Fig. 5 is the structural representation containing solid steam state thing separator of the utility model embodiment 5.
The specific embodiment
The utility model embodiment 1 is described a kind of containing solid steam state thing separator, as shown in Figure 1 and Figure 2, comprises the body 2 that contains feeding mouth 1.In described body, be provided with separate containing solid steam state thing become gaseous state, liquid state and solid-state form three area of space, the decanting zone 3 that these three area of space are the settle solids particle, with the decanting zone conducting and for separating of the condensing zone 4 of the remaining material after the processing of decanting zone, the hydrops district 5 be connected with the condensing zone conducting.Body is to be welded into an integral body 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 the condensing zone bottom is provided with condensation outlet 7, and condensing zone and hydrops district export conducting by condensation; The condensation entrance height goes out open height higher than condensation, and condensing zone top is provided with gas outlet 8, that the hydrops district is provided with is higher than condensation outlet, than condensation entrance low liquid outlet 9, the condensation entrance height is higher than the liquid outlet height, the liquid outlet height goes out open height higher than condensation.Containing solid-state steam state thing, from feeding mouth, enter, at first through decanting zone the solid sedimentation separation, steam state thing after processing enters condensing zone, in condensing zone, can close liquid outlet or be provided with in advance certain liquid object, the liquid object height exports higher than condensation, when the steam state thing except after solid enters condensing zone, after condensation, liquid object can accumulate in the hydrops district, when liquid level exports higher than condensation, just can open liquid outlet, the gaseous state thing is discharged or recycles from the gas outlet of condensing zone due to the characteristic of self, and liquid object is discharged by liquid outlet.And that the condensation entrance height goes out open height, liquid outlet higher than condensation is higher and lower than condensation entrance than the condensation outlet, these height designs that enter/export are to arrange according to the inherent characteristic of solid and steam state thing.
Further, bottom, described decanting zone is provided with the pressing device that pushes the solid precipitum.Described pressing device is included in the power set of decanting zone outer setting and the screw feeder 12 driven by power set in the bottom, decanting zone.Power set are motor 10, deceleration part 11, deceleration part and the screw feeder connection for transmission of being located on body.Motor is buncher, according to the settle solids thing the number select the speed that is applicable to output.
Further, bottom, described decanting zone is extended with the elongated area 13 that is positioned at condensing zone and below, hydrops district, and the discharge end that screw feeder is located at decanting zone and Nei， elongated area, 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 ，Bing Cong elongated area, elongated area and enters discharge nozzle, from discharge gate, discharges.
Further, the discharge gate inner bottom part is higher than elongated area discharge end inwall peak.
Further, described discharge nozzle also is provided with the seal 16 of sealing discharging mouth when first use separator.First while using separator, the seal is the sealing discharging mouth, is using separator after a period of time, can extract the seal or open out, realizes that solia particle discharges from discharge gate.The seal can be and is wound around filler, weaving filler, moulding filler or seal cover etc.
The present embodiment is changed 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 in body to be provided with two area of space of the different shapes such as separating solids and steam state, these two area of space are decanting zone 3 and condensing zone 4, the steam state thing that enters condensing zone from decanting zone is separated into gas and steam, gas is discharged from gas outlet, steam is melted in condensing zone liquid and discharges condensing zone, liquid outlet is located at condensing zone, and condensing zone has saved the condensation outlet.
The present embodiment is changed on the basis of embodiment 1, as shown in Figure 4, the body of the present embodiment and embodiment 2 is to be provided with decanting zone 3 and condensing zone 4 these two area of space equally, but embodiment 3 is that with the difference of embodiment 2 embodiment 3 has saved the setting of discharge nozzle, and the solid particle after sedimentation is directly discharged from elongated area by the conveying of screw feeder.Liquid outlet also is located at condensing zone, and condensing zone has saved the condensation outlet.
The present embodiment is changed on the basis of embodiment 1, as shown in Figure 5, the difference of this embodiment 4 and embodiment 1 is that the present embodiment 4 has additional in decanting zone and stops every the stream effect and extend containing the dividing plate 17 of the moving distance of solid steam state logistics and have additional condensate film 18 in condensing zone, this dividing plate is provided with polylith, dividing plate is for vertically being arranged in decanting zone, according to hydromechanical principle, between every dividing plate, be to there is certain difference in height between parallel longitudinal setting and adjacent separator; This condensate film is also vertical the setting.Dividing plate and condensate film not only can vertically arrange, also can horizontally set.
The above, be only preferred embodiment of the present utility model, not technology contents of the present utility model done to any pro forma restriction.Any simple modification, equivalent variations and modification that every foundation technical spirit of the present utility model is done above embodiment, all still belong in the scope of the technical solution of the utility model.
Claims (10)
1. one kind contains solid steam state thing separator, comprise the body that contains feeding mouth, it is characterized in that: be provided with at least two area of space that separate containing solid steam state thing in described body, be included in the decanting zone ,Yu decanting zone conducting that is provided with the settle solids particle in described body and for separating of decanting zone, process after the condensing zone of steam state material.
2. according to claim 1 a kind of containing solid steam state thing separator, it is characterized in that: described condensing zone is provided with the condensation entrance and is connected conducting with decanting zone, condensing zone also is provided with liquid outlet, the condensation entrance height, higher than the liquid outlet height, is provided with the gas outlet higher than condensation entrance and liquid outlet in condensing zone.
3. according to claim 2 a kind of containing solid steam state thing separator, it is characterized in that: include the hydrops district in described condensing zone, export conducting by condensation between condensing zone and hydrops district, liquid outlet is located at the hydrops district, and condensation goes out open height lower than the liquid outlet height.
4. described a kind of containing solid steam state thing separator according to claim 1-3 any one, it is characterized in that: bottom, described decanting zone is provided with and pushes the pressing device that the solid precipitum is discharged decanting zone.
5. according to claim 4 a kind of containing solid steam state thing separator, it is characterized in that: described pressing device is included in the power set of decanting zone outer setting and the screw feeder driven by power set in the decanting zone inner bottom part.
6. according to claim 5 a kind of containing solid steam state thing separator, it is characterized in that: bottom, described decanting zone is extended with the elongated area that is positioned at condensing zone and below, 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.
7. according to claim 6 a kind of 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.
8. according to claim 6 a kind of containing solid steam state thing separator, it is characterized in that: described discharge nozzle also is provided with the seal of sealing discharging mouth when first use separator.
9. according to claim 1 a kind of containing solid steam state thing separator, it is characterized in that: also be provided with in described decanting zone and stop every the stream effect and extend the dividing plate containing the moving distance of solid steam state logistics.
10. according to claim 1 a kind of containing solid steam state thing separator, it is characterized in that: also be provided with condensate film in described condensing zone.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN2013202581077U CN203315878U (en) | 2013-05-14 | 2013-05-14 | Solid-containing vaporized material separation device |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN2013202581077U CN203315878U (en) | 2013-05-14 | 2013-05-14 | Solid-containing vaporized material separation device |
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| Publication Number | Publication Date |
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| CN203315878U true CN203315878U (en) | 2013-12-04 |
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| Application Number | Title | Priority Date | Filing Date |
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| CN2013202581077U Expired - Lifetime CN203315878U (en) | 2013-05-14 | 2013-05-14 | Solid-containing vaporized material separation device |
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| Country | Link |
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| CN (1) | CN203315878U (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN103239943A (en) * | 2013-05-14 | 2013-08-14 | 陈朝阳 | Solid-containing vapor-state substance separation device |
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2013
- 2013-05-14 CN CN2013202581077U patent/CN203315878U/en not_active Expired - Lifetime
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN103239943A (en) * | 2013-05-14 | 2013-08-14 | 陈朝阳 | Solid-containing vapor-state substance separation device |
| CN103239943B (en) * | 2013-05-14 | 2015-09-23 | 陈朝阳 | Solid-containing vapor-state substance separation device |
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Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| AV01 | Patent right actively abandoned |
Granted publication date: 20131204 Effective date of abandoning: 20150923 |
|
| RGAV | Abandon patent right to avoid regrant |