CN103127739A - Inclined type gas-liquid two-stage separator for waste industrial solid organic matter granulating machine exhaust system and separation method - Google Patents
Inclined type gas-liquid two-stage separator for waste industrial solid organic matter granulating machine exhaust system and separation method Download PDFInfo
- Publication number
- CN103127739A CN103127739A CN2011103948661A CN201110394866A CN103127739A CN 103127739 A CN103127739 A CN 103127739A CN 2011103948661 A CN2011103948661 A CN 2011103948661A CN 201110394866 A CN201110394866 A CN 201110394866A CN 103127739 A CN103127739 A CN 103127739A
- Authority
- CN
- China
- Prior art keywords
- gas
- liquid
- standing separation
- separator
- chamber
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Pending
Links
Abstract
The invention provides an inclined type gas-liquid two-stage separator for waste industrial solid organic matter granulating machine exhaust system and a separation method. The inclined type gas-liquid two-stage separator consists of a gas separator and a liquid standing separator, wherein the liquid standing separator is arranged under the gas separator. An inclined separating plate divides the liquid standing separator into a standing separation chamber and an overflow chamber which are communicated through a flowing port at the lower end of the separating plate. A communicating port is arranged on the separating plate, and the standing separation chamber is communicated with the bottom of the gas separator through the communicating port and a communicating tube. Lateral walls of the standing separation chamber and the overflow chamber are provided with liquid overflowing ports, a sewage draining port is arranged at the bottom of the liquid standing separator, a high-temperature mixed gas inlet is arranged at the top of the gas separator, and the lower portion is provided with an exhaust port. A cooling water pipe is arranged in the gas separator. By means of a simple structural mode, effective separation of components in high-temperature mixed gas is finished, and gas purification and separation and resource recycling are achieved.
Description
Technical field
The present invention relates to the waste treatment device of the solid-state organic matter comminutor of a kind of waste and old industry, specifically italic formula gas-liquid two-stage separator and the separation method used of the solid-state organic matter comminutor of a kind of waste and old industry gas extraction system.
Background technology
The fast development of the solid-state organic matter industry of industry, a series of social concerns of also having brought the solid-state organic matter of discarded industry that people are unwilling to see and the useless industrial solid-state organic matter of rubbish to cause.The application of the solid-state organic matter goods of industry has been deep into the every nook and cranny of society, and from the industrial production to clothing, food, lodging and transportion--basic necessities of life, industrial solid-state organic matter goods are ubiquitous.Thereupon, the industrial solid-state organic matter rubbish of waste material in the solid-state organic matter packing material of various industry, shopping bag, plastic sheeting for farm use, woven bag, beverage bottle, industrial solid-state organic matter basin, electric appliance casing and industrial solid-state organic matter molding process etc. also constantly produces.In to the solid-state organic processing method of discarded industry, recycling is obviously best selection.In the method that discarded industrial solid-state organic matter is recycled, it is modes of commonly using as the raw material of the solid-state organic matter goods of industry that the solid-state organic matter of waste and old industry is processed into industrial solid-state organic particle through comminutor.After the solid-state organic matter of waste and old industry is processed into particle, still have good integrated materials performance, can satisfy the specification requirements such as blowing, wire drawing, trombone slide, injection moulding, extrusion profile, be widely used in industrial solid-state organic matter product enterprise.In the solid-state organic matter granulation process of industry, the waste gas of generation is all directly to discharge or deliver to the adsorption tower that adsorption solvent is housed to carry out two kinds of forms of adsorption treatment usually.The solid-state organic matter of industry is subjected to contain in thermogenetic high temperature mix waste gas a large amount of organic compositions that wait, can extract the available resources such as light oil, gasoline, diesel oil, pitch, directly discharge or directly deliver to the adsorption tower processing and not only waste adsorption solvent, cause environmental pollution or processing cost to raise, also can't effectively utilize the organic principle in discarding, cause the wasting of resources.
This shows, the italic formula gas-liquid two-stage separator that the solid-state organic matter comminutor of above-mentioned existing waste and old industry gas extraction system is used and separation method obviously still have inconvenience and defective, and demand urgently further being improved in product structure, manufacture method and use.In order to solve the problem of above-mentioned existence, relevant manufacturer there's no one who doesn't or isn't seeks solution painstakingly, but have no for a long time applicable design is completed by development always, and common product and method do not have appropriate structure and method to address the above problem, and this is obviously the problem that the anxious wish of relevant dealer solves.Therefore how to found italic formula gas-liquid two-stage separator and separation method that a kind of new solid-state organic matter comminutor of waste and old industry gas extraction system is used, real one of the current important research and development problem that belongs to, also becoming the current industry utmost point needs improved target.
Summary of the invention
main purpose of the present invention is, overcome the defective that italic formula gas-liquid two-stage separator that the solid-state organic matter comminutor of existing waste and old industry gas extraction system uses and separation method exist, and the italic formula gas-liquid two-stage separator and the separation method that provide a kind of new solid-state organic matter comminutor of waste and old industry gas extraction system to use, technical problem to be solved is that the solid-state organic matter comminutor of waste and old industry italic formula gas-liquid two-stage separator and separation method that gas extraction system is used are being provided, condensation water in the waste gas that produces in granulation process can be isolated, realize efficient utilization of resource, be very suitable for practicality.
The object of the invention to solve the technical problems realizes by the following technical solutions.its that proposes according to the present invention is comprised of gas separator (1) and liquid standing separation device (2), liquid standing separation device (2) is arranged on the below of gas separator (1), be provided with the separating plate (201) of an inclination in described liquid standing separation device (2), separating plate (201) is divided into liquid standing separation device (2) overflow chamber (203) two parts on standing separation chamber (202) and the top of bottom, standing separation chamber (202) and overflow chamber (203) are communicated with by the communication port (204) of separating plate (201) lower end, be provided with a connected entrance (205) on separating plate (201), standing separation chamber (202) is communicated with by the bottom of connected entrance (205) and communicating pipe (206) device separated from the gas (1), be equipped with overflow mouth (207) on the sidewall of standing separation chamber (202) and overflow chamber (203), be provided with sewage draining exit (208) in the bottom of liquid standing separation device (2), the main body of gas separator (1) is a gas communication pipeline that is obliquely installed, the top of gas separator (1) is provided with the high-temperature gas mixture body entrance (101) that is connected with the comminutor discharge duct, and the bottom of gas separator (1) is provided with exhaust outlet (102), the water inlet (103) that is provided with cooling-water duct, snakelike air flue, cooling water pipeline in gas separator (1) is arranged on gas separator (1) bottom, and delivery port (104) is arranged on gas separator (1) top.
The object of the invention to solve the technical problems also can be applied to the following technical measures to achieve further.
The italic formula gas-liquid two-stage separator that the solid-state organic matter comminutor of aforesaid waste and old industry gas extraction system is used, the overflow mouth (207) on the sidewall of wherein said described standing separation chamber (202) is arranged on the top of standing separation chamber (202).
The italic formula gas-liquid two-stage separator that the solid-state organic matter comminutor of aforesaid waste and old industry gas extraction system is used, the overflow mouth on the sidewall of wherein said described standing separation chamber (202) is higher than the overflow mouth on overflow chamber (203) sidewall.
The italic formula gas-liquid two-stage separator that the solid-state organic matter comminutor of aforesaid waste and old industry gas extraction system is used, wherein said described overflow mouth (207) and sewage draining exit (208) are equipped with control valve.
The object of the invention to solve the technical problems also realizes by the following technical solutions.its that proposes according to the present invention is comprised of gas separator (1) and liquid standing separation device (2), liquid standing separation device (2) is arranged on the below of gas separator (1), be provided with the separating plate (201) of an inclination in described liquid standing separation device (2), separating plate (201) is divided into liquid standing separation device (2) the standing separation chamber (overflow chamber on (202) and top (203) two parts of bottom, standing separation chamber (202) and overflow chamber (203) are communicated with by the communication port (204) of separating plate (201) lower end, be provided with a connected entrance (205) on separating plate (201), standing separation chamber (202) is communicated with by the bottom of connected entrance (205) and communicating pipe (206) device separated from the gas (1), be equipped with overflow mouth (207) on the sidewall of standing separation chamber (202) and overflow chamber (203), be provided with sewage draining exit (208) in the bottom of liquid standing separation device (2), the waste gas that is mixed with organic principle, water vapour that comminutor is discharged enters gas separator 1 from high-temperature gas mixture body entrance 101, and assembles gradually at gas separator 1, cooling final irreversible gas is from exhaust outlet 102 discharges, be provided with cooling-water duct in gas separator 1, coiled pipe air flue, the water inlet 103 of cooling-water duct are arranged on gas separator 1 bottom, and delivery port 104 is arranged on gas separator 1 top, the water that enters in the interior high-temperature gas mixture body of gas separator 1 coiled pipe air flue and cooling-water duct carries out heat exchange, heat is passed to condensed water in cooling-water duct, thereby makes the coagulable constituents such as middle organic principle, water vapour of high-temperature gas mixture body in the coiled pipe air flue be condensed into liquid, because gas separator 1 is obliquely installed, and gas is entered by the top, flow out from the bottom, mist has time enough to contact with cooling water pipeline in the process that gas separator 1 is assembled, can make the abundant condensation of condensable cost in mist, thereby effectively improve the effect of gas-liquid separation, the liquid of condensation enters in the liquid standing separation device 2 of gas separator 1 below setting from the bottom of gas separator 1, the mixing material that condenses in gas separator 1 is by entering standing separation chamber 202 communicating pipe 206, because the proportion of each composition of mixing material is different, layering appears in each composition after standing separation chamber 202 interior processes are standing, the light oil on upper strata is gathered in 202 tops, standing separation chamber, more heavier composition enters overflow chamber 203 by communication port 204 after sinking, and the heaviest composition is deposited in the bottom of liquid standing separation device 2, be equipped with overflow mouth 207 on the sidewall of standing separation chamber 202 and overflow chamber 203, the setting position of overflow mouth 207 is provided with sewage draining exit 208 higher than the upper edge of communication port 204 in the bottom of liquid standing separation device 2, overflow mouth 207 on 202 sidewalls of standing separation chamber is arranged on the top of standing separation chamber 202, and the overflow mouth on 202 sidewalls of standing separation chamber is higher than the overflow mouth on overflow chamber's 203 sidewalls, component at liquid standing separation device 2 interior isolated different specific weights is discharged by corresponding overflow mouth 207 or sewage draining exit 208 respectively, and collects and utilize.
By technique scheme; italic formula gas-liquid two-stage separator and separation method that the solid-state organic matter comminutor of the waste and old industry of the present invention gas extraction system is used have following advantages and beneficial effect at least: the high-temperature gas mixture body that the solid-state organic matter of waste and old industry produces when granulation makes the condensable components condense in mist become liquid and separated by the condensation of gas separator.Isolated liquid component is standing demix in liquid standing separation device, by the compartmentation of separating plate, the component of the different specific weight of separating out is flowed out by corresponding outlet.Because gas separator is obliquely installed, and gas is entered by the top, flows out from the bottom, and mist has time enough to contact with cooling water pipeline in the process that gas separator is assembled, can make the abundant condensation of condensable cost in mist, thereby effectively improve the effect of gas-liquid separation.By simple frame mode, completed effective separation of a component in the high temperature mix waste gas in the solid-state organic matter granulation process of waste and old industry, realized the recycling of gas cleaning, separation and resource.Compact equipment occupies little space; Equipment maintenance cost is low, and manufacturing cost reduces relatively, thereby can significantly reduce operating cost, improves the economy and environment benefit.
In sum, italic formula gas-liquid two-stage separator and separation method that the solid-state organic matter comminutor of the waste and old industry of the present invention gas extraction system is used are comprised of gas separator and liquid standing separation device, and liquid standing separation device is located at below gas separator; The separating plate of an inclination is divided into standing separation chamber and overflow chamber's two parts with liquid standing separation device, standing separation chamber and overflow chamber are communicated with by the communication port of separating plate lower end, separating plate is provided with connected entrance, and the standing separation chamber is communicated with by connected entrance and communicating pipe device separated from the gas bottom; Be equipped with the overflow mouth on the sidewall of standing separation chamber and overflow chamber, liquid standing separation device bottom is provided with sewage draining exit, the gas separator main body is a gas communication pipeline that is obliquely installed, and the gas separator top is provided with high-temperature gas mixture body entrance, and the bottom is provided with exhaust outlet; Be provided with cooling water pipeline in gas separator.By simple frame mode, completed effective separation of a component in the high temperature mix waste gas in the solid-state organic matter granulation process of waste and old industry, realized the recycling of gas cleaning, separation and resource.The present invention has significant progress technically, and has obvious good effect, is really a new and innovative, progressive, practical new design.
Above-mentioned explanation is only the general introduction of technical solution of the present invention, for can clearer understanding technological means of the present invention, and can be implemented according to the content of specification, and for above and other purpose of the present invention, feature and advantage can be become apparent, below especially exemplified by preferred embodiment, and the cooperation accompanying drawing, be described in detail as follows.
Description of drawings
Fig. 1 is structural representation of the present invention.
1: gas separator 101: high-temperature gas mixture body entrance
102: exhaust outlet 103: water inlet
104: delivery port 2: liquid standing separation device
201: separating plate 202: the standing separation chamber
203: overflow chamber 204: communication port
205: connected entrance 206: communicating pipe
207: overflow mouth 208: sewage draining exit
The specific embodiment
Reach for further setting forth the present invention technological means and the effect that predetermined goal of the invention is taked; below in conjunction with accompanying drawing and preferred embodiment; italic formula gas-liquid two-stage separator and its specific embodiment of separation method, structure, manufacture method, step, feature and effect thereof to the solid-state organic matter comminutor of the waste and old industry gas extraction system of foundation the present invention proposition is used are described in detail as follows.
Italic formula gas-liquid two-stage separator and separation method that the solid-state organic matter comminutor of a kind of waste and old industry gas extraction system is used; formed by gas separator 1 and liquid standing separation device 2; the main body of gas separator 1 is a gas communication pipeline that is obliquely installed; the top of gas separator 1 is provided with the high-temperature gas mixture body entrance 101 that is connected with the comminutor discharge duct, and the bottom of gas separator 1 is provided with exhaust outlet 102.The waste gas that is mixed with organic principle, water vapour that comminutor is discharged enters gas separator 1 from high-temperature gas mixture body entrance 101, and assembles gradually at gas separator 1, cooling final irreversible gas is from exhaust outlet 102 discharges.Be provided with cooling-water duct in gas separator 1, coiled pipe air flue, the water inlet 103 of cooling-water duct are arranged on gas separator 1 bottom, and delivery port 104 is arranged on gas separator 1 top.The water that enters in the interior high-temperature gas mixture body of gas separator 1 coiled pipe air flue and cooling-water duct carries out heat exchange, heat is passed to condensed water in cooling-water duct, thereby makes the coagulable constituents such as middle organic principle, water vapour of high-temperature gas mixture body in the coiled pipe air flue be condensed into liquid.Because gas separator 1 is obliquely installed, and gas is entered by the top, flow out from the bottom, mist has time enough to contact with cooling water pipeline in the process that gas separator 1 is assembled, can make the abundant condensation of condensable cost in mist, thereby effectively improve the effect of gas-liquid separation.The liquid of condensation enters in the liquid standing separation device 2 of gas separator 1 below setting from the bottom of gas separator 1.
Be provided with the separating plate 201 of an inclination in described liquid standing separation device 2, separating plate 201 is divided into liquid standing separation device 2 overflow chamber's 203 two parts on standing separation chamber 202 and the top of bottom, be provided with a connected entrance 205 on separating plate 201, standing separation chamber 202 by connected entrance 205 and communicating pipe 206 device 1 separated from the gas the bottom be communicated with; Standing separation chamber 202 and overflow chamber 203 is communicated with communication port 204 between liquid standing separation device 2 inwalls by separating plate 201 lower ends.Condense mixing material by entering standing separation chamber 202 communicating pipe 206 in gas separator 1, because the proportion of each composition of mixing material is different, layering appears in each composition after standing separation chamber 202 interior processes are standing, the light oil on upper strata is gathered in 202 tops, standing separation chamber, more heavier composition enters overflow chamber 203 by communication port 204 after sinking, and the heaviest composition is deposited in the bottom of liquid standing separation device 2.Be equipped with overflow mouth 207 on the sidewall of standing separation chamber 202 and overflow chamber 203, the setting position of overflow mouth 207 is provided with sewage draining exit 208 higher than the upper edge of communication port 204 in the bottom of liquid standing separation device 2.Overflow mouth 207 on 202 sidewalls of standing separation chamber is arranged on the top of standing separation chamber 202, and the overflow mouth on 202 sidewalls of standing separation chamber is higher than the overflow mouth on overflow chamber's 203 sidewalls.Component at liquid standing separation device 2 interior isolated different specific weights is discharged by corresponding overflow mouth 207 or sewage draining exit 208 respectively, and collects and utilize.
Described overflow mouth 207 and sewage draining exit 208 are equipped with control valve.
The above is optimum embodiment of the present invention; in addition; the waste gas that is mixed with organic principle, water vapour that comminutor is discharged enters gas separator 1 from high-temperature gas mixture body entrance 101, and assembles gradually at gas separator 1, cooling final irreversible gas is from exhaust outlet 102 discharges.Be provided with cooling-water duct in gas separator 1, coiled pipe air flue, the water inlet 103 of cooling-water duct are arranged on gas separator 1 bottom, and delivery port 104 is arranged on gas separator 1 top.The water that enters in the interior high-temperature gas mixture body of gas separator 1 coiled pipe air flue and cooling-water duct carries out heat exchange, heat is passed to condensed water in cooling-water duct, thereby makes the coagulable constituents such as middle organic principle, water vapour of high-temperature gas mixture body in the coiled pipe air flue be condensed into liquid.Because gas separator 1 is obliquely installed, and gas is entered by the top, flow out from the bottom, mist has time enough to contact with cooling water pipeline in the process that gas separator 1 is assembled, can make the abundant condensation of condensable cost in mist, thereby effectively improve the effect of gas-liquid separation.The liquid of condensation enters in the liquid standing separation device 2 of gas separator 1 below setting from the bottom of gas separator 1.
The mixing material that condenses in gas separator 1 is by entering standing separation chamber 202 communicating pipe 206, because the proportion of each composition of mixing material is different, layering appears in each composition after standing separation chamber 202 interior processes are standing, the light oil on upper strata is gathered in 202 tops, standing separation chamber, more heavier composition enters overflow chamber 203 by communication port 204 after sinking, and the heaviest composition is deposited in the bottom of liquid standing separation device 2.Be equipped with overflow mouth 207 on the sidewall of standing separation chamber 202 and overflow chamber 203, the setting position of overflow mouth 207 is provided with sewage draining exit 208 higher than the upper edge of communication port 204 in the bottom of liquid standing separation device 2.Overflow mouth 207 on 202 sidewalls of standing separation chamber is arranged on the top of standing separation chamber 202, and the overflow mouth on 202 sidewalls of standing separation chamber is higher than the overflow mouth on overflow chamber's 203 sidewalls.Component at liquid standing separation device 2 interior isolated different specific weights is discharged by corresponding overflow mouth 207 or sewage draining exit 208 respectively, and collects and utilize.
the above, it is only preferred embodiment of the present invention, be not that the present invention is done any pro forma restriction, although the present invention discloses as above with preferred embodiment, yet be not to limit the present invention, any those skilled in the art, within not breaking away from the technical solution of the present invention scope, when the method that can utilize above-mentioned announcement and technology contents are made a little change or be modified to the equivalent embodiment of equivalent variations, in every case be the content that does not break away from technical solution of the present invention, any simple modification that foundation technical spirit of the present invention is done above embodiment, equivalent variations and modification, all still belong in the scope of technical solution of the present invention.
Claims (5)
1. italic formula gas-liquid two-stage separator that the solid-state organic matter comminutor of waste and old industry gas extraction system is used, it is comprised of gas separator and liquid standing separation device, liquid standing separation device is arranged on the below of gas separator, be provided with the separating plate of an inclination in described liquid standing separation device, separating plate is divided into liquid standing separation device overflow chamber's two parts on standing separation chamber and the top of bottom, standing separation chamber and overflow chamber are communicated with by the communication port of separating plate lower end, be provided with a connected entrance on separating plate, the standing separation chamber by connected entrance and communicating pipe device separated from the gas the bottom be communicated with, be equipped with the overflow mouth on the sidewall of standing separation chamber and overflow chamber, be provided with sewage draining exit in the bottom of liquid standing separation device,
It is characterized in that: the main body of gas separator is a gas communication pipeline that is obliquely installed, and the top of gas separator is provided with the high-temperature gas mixture body entrance that is connected with the comminutor discharge duct, and the bottom of gas separator is provided with exhaust outlet; The water inlet that is provided with cooling-water duct, snakelike air flue, cooling water pipeline in gas separator is arranged on the gas separator bottom, and delivery port is arranged on gas separator top.
2. the italic formula gas-liquid two-stage separator used of the solid-state organic matter comminutor of waste and old industry as claimed in claim 1 gas extraction system is characterized in that: the overflow mouth on the sidewall of described standing separation chamber is arranged on the top of standing separation chamber.
3. the italic formula gas-liquid two-stage separator used of the solid-state organic matter comminutor of waste and old industry as claimed in claim 1 gas extraction system is characterized in that: the overflow mouth on the sidewall of described standing separation chamber is higher than the overflow mouth on overflow chamber's sidewall.
4. the italic formula gas-liquid two-stage separator used of the solid-state organic matter comminutor of waste and old industry as claimed in claim 1 gas extraction system, it is characterized in that: described overflow mouth and sewage draining exit are equipped with control valve.
5. the separation method of the italic formula gas-liquid two-stage separator used of the solid-state organic matter comminutor of a waste and old industry gas extraction system, it is comprised of gas separator and liquid standing separation device, liquid standing separation device is arranged on the below of gas separator, be provided with the separating plate of an inclination in described liquid standing separation device, separating plate is divided into liquid standing separation device overflow chamber's two parts on standing separation chamber and the top of bottom, standing separation chamber and overflow chamber are communicated with by the communication port of separating plate lower end, be provided with a connected entrance on separating plate, the standing separation chamber by connected entrance and communicating pipe device separated from the gas the bottom be communicated with, be equipped with the overflow mouth on the sidewall of standing separation chamber and overflow chamber, be provided with sewage draining exit in the bottom of liquid standing separation device,
It is characterized in that, the waste gas that is mixed with organic principle, water vapour that comminutor is discharged enters gas separator from high-temperature gas mixture body entrance, and assemble gradually at gas separator, cooling final irreversible gas discharges from exhaust outlet; Be provided with cooling-water duct in gas separator, coiled pipe air flue, the water inlet of cooling-water duct are arranged on the gas separator bottom, and delivery port is arranged on gas separator top; The water that enters in the interior high-temperature gas mixture body of gas separator coiled pipe air flue and cooling-water duct carries out heat exchange, heat is passed to condensed water in cooling-water duct, thereby makes the coagulable constituents such as middle organic principle, water vapour of high-temperature gas mixture body in the coiled pipe air flue be condensed into liquid; Because gas separator is obliquely installed, and gas is entered by the top, flows out from the bottom, and mist has time enough to contact with cooling water pipeline in the process that gas separator is assembled, can make the abundant condensation of condensable cost in mist, thereby effectively improve the effect of gas-liquid separation; The liquid of condensation enters in the liquid standing separation device of gas separator below setting from the bottom of gas separator,
The mixing material that condenses in gas separator is by entering the standing separation chamber communicating pipe, because the proportion of each composition of mixing material is different, layering appears in each composition after the indoor process of standing separation is standing, the light oil on upper strata is gathered in top, standing separation chamber, more heavier composition enters the overflow chamber by communication port after sinking, and the heaviest composition is deposited in the bottom of liquid standing separation device; Be equipped with the overflow mouth on the sidewall of standing separation chamber and overflow chamber, the setting position of overflow mouth is provided with sewage draining exit higher than the upper edge of communication port in the bottom of liquid standing separation device; Overflow mouth on the sidewall of standing separation chamber is arranged on the top of standing separation chamber, and the overflow mouth on the sidewall of standing separation chamber is higher than the overflow mouth on overflow chamber's sidewall; The component of isolated different specific weight is discharged by corresponding overflow mouth or sewage draining exit respectively in liquid standing separation device, and collects and utilize.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN2011103948661A CN103127739A (en) | 2011-12-02 | 2011-12-02 | Inclined type gas-liquid two-stage separator for waste industrial solid organic matter granulating machine exhaust system and separation method |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN2011103948661A CN103127739A (en) | 2011-12-02 | 2011-12-02 | Inclined type gas-liquid two-stage separator for waste industrial solid organic matter granulating machine exhaust system and separation method |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN103127739A true CN103127739A (en) | 2013-06-05 |
Family
ID=48488574
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN2011103948661A Pending CN103127739A (en) | 2011-12-02 | 2011-12-02 | Inclined type gas-liquid two-stage separator for waste industrial solid organic matter granulating machine exhaust system and separation method |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN103127739A (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN107421691A (en) * | 2017-08-28 | 2017-12-01 | 西北工业大学 | A kind of fuel tank low temperature airtightness reliability test system and method |
Citations (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN201049219Y (en) * | 2007-06-15 | 2008-04-23 | 上海市闵行中学 | Oil-water separator |
| JP2010131516A (en) * | 2008-12-04 | 2010-06-17 | Panasonic Corp | Oil-water separator |
| CN201701774U (en) * | 2009-12-22 | 2011-01-12 | 上海闰铭精密技术有限公司 | Organic gas condensing and recycling device |
| CN102430259A (en) * | 2011-11-21 | 2012-05-02 | 洛阳骏腾能源科技有限公司 | Inclined gas-liquid two-stage separator for waste plastic granulator and separation method for inclined gas-liquid two-stage separator |
| CN202410212U (en) * | 2011-12-02 | 2012-09-05 | 洛阳骏腾能源科技有限公司 | Oblique gas-liquid two-stage separator for exhaust system of waste industrial solid organic matter pelletizer |
-
2011
- 2011-12-02 CN CN2011103948661A patent/CN103127739A/en active Pending
Patent Citations (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN201049219Y (en) * | 2007-06-15 | 2008-04-23 | 上海市闵行中学 | Oil-water separator |
| JP2010131516A (en) * | 2008-12-04 | 2010-06-17 | Panasonic Corp | Oil-water separator |
| CN201701774U (en) * | 2009-12-22 | 2011-01-12 | 上海闰铭精密技术有限公司 | Organic gas condensing and recycling device |
| CN102430259A (en) * | 2011-11-21 | 2012-05-02 | 洛阳骏腾能源科技有限公司 | Inclined gas-liquid two-stage separator for waste plastic granulator and separation method for inclined gas-liquid two-stage separator |
| CN202410212U (en) * | 2011-12-02 | 2012-09-05 | 洛阳骏腾能源科技有限公司 | Oblique gas-liquid two-stage separator for exhaust system of waste industrial solid organic matter pelletizer |
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN107421691A (en) * | 2017-08-28 | 2017-12-01 | 西北工业大学 | A kind of fuel tank low temperature airtightness reliability test system and method |
| CN107421691B (en) * | 2017-08-28 | 2020-07-07 | 西北工业大学 | Oil tank low-temperature air tightness reliability test system and method |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| CN102430259B (en) | Inclined gas-liquid two-stage separator for waste plastic granulator and separation method for inclined gas-liquid two-stage separator | |
| CN102407027B (en) | Gas-liquid two-stage separator and separation method for waste and old plastic granulator | |
| CN202410212U (en) | Oblique gas-liquid two-stage separator for exhaust system of waste industrial solid organic matter pelletizer | |
| CN202398131U (en) | Inclined type gas-liquid two-stage separator for waste plastic granulating machine | |
| CN103127739A (en) | Inclined type gas-liquid two-stage separator for waste industrial solid organic matter granulating machine exhaust system and separation method | |
| CN202398132U (en) | Gas-liquid two-stage separator for waste plastic granulating machine | |
| CN202410213U (en) | Gas-liquid two-stage separator for exhaust system of waste industrial solid organic matter pelletizer | |
| CN205796855U (en) | A kind of high-efficient wet-type organic abnormal flavour waste gas purification cleaner unit | |
| CN107035658A (en) | Oily after-treatment device and vavuum pump | |
| CN103143187A (en) | Gas-liquid two-stage separator for exhaust system of waste industrial solid organic material pelletizer | |
| CN105585193A (en) | Water inlet mechanism of wastewater treatment equipment | |
| CN101830627B (en) | Sludge vibrating mixing spouted bed drying device and method | |
| CN203043804U (en) | Organic waste gas recycling and purifying device | |
| CN204661634U (en) | A kind of Mobile lubrication oil three combined dehydration devices | |
| CN103965508A (en) | Reclaimed rubber desulfurization device and reclaimed rubber desulfurization method both capable of treating smoke by use of vacuum smoke elimination method | |
| CN103239943B (en) | Solid-containing vapor-state substance separation device | |
| CN203954969U (en) | Water smoke air purifier | |
| CN203315878U (en) | Solid-containing vaporized material separation device | |
| CN203170062U (en) | Device for separating oil from water | |
| CN202803070U (en) | Formaldehyde absorption tower capable of recycling amino-plastic wastewater | |
| CN203208711U (en) | Flash tank | |
| CN202342939U (en) | Alcohol secondary recovering tower | |
| CN105056695A (en) | Furfural gas and residue separation and recovery device and recovery method | |
| CN104890144A (en) | Environment-friendly granulator for waste plastic recovery | |
| CN203829853U (en) | Upward spray and inward negative pressure type desulfurization dust removal device |
Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C06 | Publication | ||
| PB01 | Publication | ||
| C10 | Entry into substantive examination | ||
| SE01 | Entry into force of request for substantive examination | ||
| C02 | Deemed withdrawal of patent application after publication (patent law 2001) | ||
| WD01 | Invention patent application deemed withdrawn after publication |
Application publication date: 20130605 |