CN202410212U - Oblique gas-liquid two-stage separator for exhaust system of waste industrial solid organic matter pelletizer - Google Patents
Oblique gas-liquid two-stage separator for exhaust system of waste industrial solid organic matter pelletizer Download PDFInfo
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- CN202410212U CN202410212U CN2011204952091U CN201120495209U CN202410212U CN 202410212 U CN202410212 U CN 202410212U CN 2011204952091 U CN2011204952091 U CN 2011204952091U CN 201120495209 U CN201120495209 U CN 201120495209U CN 202410212 U CN202410212 U CN 202410212U
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Abstract
The utility model discloses an oblique gas-liquid two-stage separator for an exhaust system of a waste industrial solid organic matter pelletizer. The oblique gas-liquid two-stage separator consists of a gas separator and a liquid standing separator, wherein the liquid standing separator is arranged below the gas separator; an oblique separating plate is used for partitioning the liquid standing separator into a standing separating chamber and an overflow chamber; the standing separating chamber and the overflow chamber are communicated with each other through a flow port at the lower end of the separating plate; the separating plate is provided with a communicating port; the standing separating chamber is communicated with the bottom of the gas separator through the communicating port and a communicating pipe; the side walls of the standing separating chamber and the overflow chamber are provided with liquid overflow ports; the bottom of the liquid standing separator is provided with a drain outlet; the top of the gas separator is provided with a high-temperature mixed gas inlet; the lower part of the gas separator is provided with an exhaust port; and a cooling water pipeline is arranged in the gas separator. Through a simple structural way, effective separation of components in a high-temperature mixed waste gas is completed, and purification and separation of gases and recycling of resources are realized.
Description
Technical field
The present invention relates to a kind of waste treatment device of waste and old industrial solid organic thing comminutor, the italic formula gas-liquid two-stage separator that specifically a kind of waste and old industrial solid organic thing comminutor gas extraction system is used.
Background technology
The fast development of industry solid organic thing industry, a series of social concerns of also having brought discarded industrial solid organic thing that people are unwilling to see and the useless industrial solid organic thing of rubbish to cause.The application of industry solid organic Tetramune has been deep into the every nook and cranny of society, and from the commercial production to clothing, food, lodging and transportion--basic necessities of life, industrial solid organic Tetramune is ubiquitous.Thereupon, the industrial solid organic thing rubbish of waste material in various industrial solid organic thing packing materials, shopping bag, plastic sheeting for farm use, woven bag, beverage bottle, industrial solid organic thing basin, electric appliance casing and the industrial solid organic thing molding process or the like also constantly produces.In the processing method to discarded industrial solid organic thing, recycling obviously is a best choice.In the method that discarded industrial solid organic thing is recycled, it is the mode of using always as the raw material of industrial solid organic Tetramune that waste and old industrial solid organic thing is processed into industrial solid organic composition granule through comminutor.After waste and old industrial solid organic thing is processed into particle, still have good integrated materials performance, can satisfy specification requirements such as blowing, wire drawing, trombone slide, injection moulding, extrusion profile, be widely used in industrial solid organic Tetramune enterprise.In industrial solid organic thing granulation process, the waste gas of generation all is 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.Industry solid organic thing receives to contain in the thermogenetic high temperature mix waste gas a large amount of organic compositions that wait; Can extract 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 that the italic formula gas-liquid two-stage separator that above-mentioned existing waste and old industrial solid organic thing comminutor gas extraction system is used obviously still has inconvenience and defective, and demands urgently further improving in product structure, manufacturing approach 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 do not see always that for a long time suitable design is developed completion; And common product and method do not have appropriate structure and method to address the above problem, and this obviously is the problem that the anxious desire of relevant dealer solves.Therefore how to found the italic formula gas-liquid two-stage separator that a kind of new waste and old industrial solid organic thing comminutor 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 existing waste and old industrial solid organic thing comminutor gas extraction system uses exists; And the italic formula gas-liquid two-stage separator that provides a kind of new waste and old industrial solid organic thing comminutor gas extraction system to use; Technical problem to be solved is at the italic formula gas-liquid two-stage separator that provides waste and old industrial solid organic thing comminutor gas extraction system to use; Can the condensation water in the waste gas that produce in the granulation process be isolated, realize the resources effective utilization, be very suitable for practicality.
The object of the invention and solve its technical problem and adopt following technical scheme to realize.Its that proposes according to the present invention is made up 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 the described liquid standing separation device (2); Separating plate (201) is divided into liquid standing separation device (2) overflow chamber (203) two parts on the standing separation chamber (202) and the top of bottom; Standing separation chamber (202) and overflow chamber (203) are communicated with through the communication port (204) of separating plate (201) lower end; On separating plate (201), be provided with a connected entrance (205), standing separation chamber (202) are communicated with through the bottom of connected entrance (205) and communicating pipe (206) device separated from the gas (1); On the sidewall of standing separation chamber (202) and overflow chamber (203), be equipped with liquid overfall (207); 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 inlet (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 in gas separator (1), is provided with cooling-water duct, snakelike air flue, cooling water pipeline is arranged on gas separator (1) bottom, and delivery port (104) is arranged on gas separator (1) top.
The object of the invention and solve its technical problem and also can adopt following technical measures further to realize.
The italic formula gas-liquid two-stage separator that aforesaid waste and old industrial solid organic thing comminutor gas extraction system is used, the liquid overfall (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 aforesaid waste and old industrial solid organic thing comminutor gas extraction system is used, the liquid overfall on the sidewall of wherein said said standing separation chamber (202) is higher than the liquid overfall on overflow chamber (203) sidewall.
The italic formula gas-liquid two-stage separator that aforesaid waste and old industrial solid organic thing comminutor gas extraction system is used, wherein said described liquid overfall (207) and sewage draining exit (208) are equipped with control valve.
The object of the invention and solve its technical problem and also adopt following technical scheme to realize.Its that proposes according to the present invention is made up 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 the 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 through the communication port (204) of separating plate (201) lower end; On separating plate (201), be provided with a connected entrance (205), standing separation chamber (202) are communicated with through the bottom of connected entrance (205) and communicating pipe (206) device separated from the gas (1); On the sidewall of standing separation chamber (202) and overflow chamber (203), be equipped with liquid overfall (207); 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 gets into gas separator 1 from high-temperature gas mixture body inlet 101, and assembles, cools off final irreversible gas gradually at gas separator 1 and discharge from exhaust outlet 102; In gas separator 1, be provided with cooling-water duct, the coiled pipe air flue, the water inlet 103 of cooling-water duct is arranged on gas separator 1 bottom, and delivery port 104 is arranged on gas separator 1 top; The water that gets in interior high-temperature gas mixture body of gas separator 1 coiled pipe air flue and the cooling-water duct carries out heat exchange; Heat is passed to the condensed water in the 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 got into 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, and can make the abundant condensation of condensable cost in the mist, thereby effectively improve the effect of gas-liquid separation; The liquid of condensation gets in the liquid standing separation device 2 of gas separator 1 below setting from the bottom of gas separator 1; The mixing material that in gas separator 1, condenses gets into standing separation chamber 202 through communicating pipe 206; Because the proportion of each composition of mixing material is different; In standing separation chamber 202 through leaving standstill each composition of back layering appears; The light oil on upper strata accumulates in 202 tops, standing separation chamber, and heavier composition sinks the back through communication port 204 entering overflow chambers 203, and the heaviest composition then is deposited in the bottom of liquid standing separation device 2; On the sidewall of standing separation chamber 202 and overflow chamber 203, be equipped with liquid overfall 207, liquid overfall 207 the upper edge that the position is higher than communication port 204 is set, be provided with sewage draining exit 208 in the bottom of liquid standing separation device 2; Liquid overfall 207 on 202 sidewalls of standing separation chamber is arranged on the top of standing separation chamber 202, and the liquid overfall on 202 sidewalls of standing separation chamber is higher than the liquid overfall on overflow chamber's 203 sidewalls; The component of isolated different specific weight is discharged through corresponding liquid overfall 207 or sewage draining exit 208 respectively in liquid standing separation device 2, and collects and utilize.
By technique scheme; The italic formula gas-liquid two-stage separator that the waste and old industrial solid organic thing comminutor gas extraction system of the present invention is used has advantage and beneficial effect at least: the high-temperature gas mixture body that waste and old industrial solid organic thing produces when granulation makes the condensable components condense in the mist become liquid and separated through the condensation of gas separator.Isolated liquid component is standing demix in liquid standing separation device, through the compartmentation of separating plate, the component of the different specific weight of separating out is flowed out through corresponding outlet.Because gas separator is obliquely installed; And gas is got into 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 the mist, thereby effectively improve the effect of gas-liquid separation.Through simple frame mode, accomplished effective separation of a component in the high temperature mix waste gas in the waste and old industrial solid organic thing granulation process, 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 economy and environmental benefit.
In sum, the italic formula gas-liquid two-stage separator that the waste and old industrial solid organic thing comminutor gas extraction system of the present invention is used is made up of gas separator and liquid standing separation device, and liquid standing separation device is located at the gas separator below; 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 through the communication port of separating plate lower end; Separating plate is provided with connected entrance, and the standing separation chamber is through connected entrance and communicating pipe device separated from the gas bottom connection; Be equipped with the liquid overfall 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 inlet, and the bottom is provided with exhaust outlet; Be provided with cooling water pipeline in the gas separator.Through simple frame mode, accomplished effective separation of a component in the high temperature mix waste gas in the waste and old industrial solid organic thing granulation process, realized the recycling of gas cleaning, separation and resource.The present invention has obvious improvement technically, and has tangible good effect, really is the new design of a novelty, progress, practicality.
Above-mentioned explanation only is the general introduction of technical scheme of the present invention; Understand technological means of the present invention in order can more to know; And can implement according to the content of specification, and for let of the present invention above-mentioned with other purposes, feature and advantage can be more obviously understandable, below special act preferred embodiment; And conjunction with figs., specify as follows.
Description of drawings
Fig. 1 is a structural representation of the present invention.
1: gas separator 101: high-temperature gas mixture body inlet
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: liquid overfall 208: sewage draining exit
The specific embodiment
Reach technological means and the effect that predetermined goal of the invention is taked for further setting forth the present invention; Below in conjunction with accompanying drawing and preferred embodiment; To its specific embodiment of italic formula gas-liquid two-stage separator, structure, manufacturing approach, step, characteristic and the effect thereof that the waste and old industrial solid organic thing comminutor gas extraction system that proposes according to the present invention is used, specify as after.
The italic formula gas-liquid two-stage separator that a kind of waste and old industrial solid organic thing comminutor gas extraction system is used; Form 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 inlet 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 gets into gas separator 1 from high-temperature gas mixture body inlet 101, and assembles, cools off final irreversible gas gradually at gas separator 1 and discharge from exhaust outlet 102.In gas separator 1, be provided with cooling-water duct, the coiled pipe air flue, the water inlet 103 of cooling-water duct is arranged on gas separator 1 bottom, and delivery port 104 is arranged on gas separator 1 top.The water that gets in interior high-temperature gas mixture body of gas separator 1 coiled pipe air flue and the cooling-water duct carries out heat exchange; Heat is passed to the condensed water in the 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 got into 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, and can make the abundant condensation of condensable cost in the mist, thereby effectively improve the effect of gas-liquid separation.The liquid of condensation gets 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 the described liquid standing separation device 2; Separating plate 201 is divided into liquid standing separation device 2 overflow chamber's 203 two parts on the standing separation chamber 202 and the top of bottom; On separating plate 201, be provided with a connected entrance 205, standing separation chamber 202 is through the bottom connection of connected entrance 205 with communicating pipes 206 device 1 separated from the gas; Standing separation chamber 202 and overflow chamber 203 is communicated with communication port 204 between liquid standing separation device 2 inwalls through separating plate 201 lower ends.The mixing material that in gas separator 1, condenses gets into standing separation chamber 202 through communicating pipe 206; Because the proportion of each composition of mixing material is different; In standing separation chamber 202 through leaving standstill each composition of back layering appears; The light oil on upper strata accumulates in 202 tops, standing separation chamber, and heavier composition sinks the back through communication port 204 entering overflow chambers 203, and the heaviest composition then is deposited in the bottom of liquid standing separation device 2.On the sidewall of standing separation chamber 202 and overflow chamber 203, be equipped with liquid overfall 207, liquid overfall 207 the upper edge that the position is higher than communication port 204 is set, be provided with sewage draining exit 208 in the bottom of liquid standing separation device 2.Liquid overfall 207 on 202 sidewalls of standing separation chamber is arranged on the top of standing separation chamber 202, and the liquid overfall on 202 sidewalls of standing separation chamber is higher than the liquid overfall on overflow chamber's 203 sidewalls.The component of isolated different specific weight is discharged through corresponding liquid overfall 207 or sewage draining exit 208 respectively in liquid standing separation device 2, and collects and utilize.
Described liquid overfall 207 is equipped with control valve with sewage draining exit 208.
The above is an optimum embodiment of the present invention; In addition; The waste gas that is mixed with organic principle, water vapour that comminutor is discharged gets into gas separator 1 from high-temperature gas mixture body inlet 101, and assembles, cools off final irreversible gas gradually at gas separator 1 and discharge from exhaust outlet 102.In gas separator 1, be provided with cooling-water duct, the coiled pipe air flue, the water inlet 103 of cooling-water duct is arranged on gas separator 1 bottom, and delivery port 104 is arranged on gas separator 1 top.The water that gets in interior high-temperature gas mixture body of gas separator 1 coiled pipe air flue and the cooling-water duct carries out heat exchange; Heat is passed to the condensed water in the 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 got into 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, and can make the abundant condensation of condensable cost in the mist, thereby effectively improve the effect of gas-liquid separation.The liquid of condensation gets in the liquid standing separation device 2 of gas separator 1 below setting from the bottom of gas separator 1.
The mixing material that in gas separator 1, condenses gets into standing separation chamber 202 through communicating pipe 206; Because the proportion of each composition of mixing material is different; In standing separation chamber 202 through leaving standstill each composition of back layering appears; The light oil on upper strata accumulates in 202 tops, standing separation chamber, and heavier composition sinks the back through communication port 204 entering overflow chambers 203, and the heaviest composition then is deposited in the bottom of liquid standing separation device 2.On the sidewall of standing separation chamber 202 and overflow chamber 203, be equipped with liquid overfall 207, liquid overfall 207 the upper edge that the position is higher than communication port 204 is set, be provided with sewage draining exit 208 in the bottom of liquid standing separation device 2.Liquid overfall 207 on 202 sidewalls of standing separation chamber is arranged on the top of standing separation chamber 202, and the liquid overfall on 202 sidewalls of standing separation chamber is higher than the liquid overfall on overflow chamber's 203 sidewalls.The component of isolated different specific weight is discharged through corresponding liquid overfall 207 or sewage draining exit 208 respectively in liquid standing separation device 2, and collects and utilize.
The above only is preferred embodiment of the present invention, is not the present invention is done any pro forma restriction; Though the present invention discloses as above with preferred embodiment; Yet be not in order to limiting the present invention, anyly be familiar with the professional and technical personnel, in not breaking away from technical scheme scope of the present invention; When the method for above-mentioned announcement capable of using 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 scheme of the present invention, to any simple modification, equivalent variations and modification that above embodiment did, all still belong in the scope of technical scheme of the present invention according to technical spirit of the present invention.
Claims (4)
1. italic formula gas-liquid two-stage separator that waste and old industrial solid organic thing comminutor gas extraction system is used; It is made up 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 the described liquid standing separation device, separating plate is divided into overflow chamber's two parts on the standing separation chamber and the top of bottom with liquid standing separation device, and standing separation chamber and overflow chamber are communicated with through the communication port of separating plate lower end; On separating plate, be provided with a connected entrance, the standing separation chamber is through the bottom connection of connected entrance with communicating pipe device separated from the gas; On the sidewall of standing separation chamber and overflow chamber, be equipped with the liquid overfall, 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 inlet that is connected with the comminutor discharge duct, and the bottom of gas separator is provided with exhaust outlet; The water inlet that in gas separator, is provided with cooling-water duct, snakelike air flue, cooling water pipeline 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 that waste and old industrial solid organic thing comminutor gas extraction system as claimed in claim 1 is used, it is characterized in that: the liquid overfall 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 that waste and old industrial solid organic thing comminutor gas extraction system as claimed in claim 1 is used, it is characterized in that: the liquid overfall on the sidewall of said standing separation chamber is higher than the liquid overfall on overflow chamber's sidewall.
4. the italic formula gas-liquid two-stage separator that waste and old industrial solid organic thing comminutor gas extraction system as claimed in claim 1 is used, it is characterized in that: described liquid overfall and sewage draining exit are equipped with control valve.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN2011204952091U CN202410212U (en) | 2011-12-02 | 2011-12-02 | Oblique gas-liquid two-stage separator for exhaust system of waste industrial solid organic matter pelletizer |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN2011204952091U CN202410212U (en) | 2011-12-02 | 2011-12-02 | Oblique gas-liquid two-stage separator for exhaust system of waste industrial solid organic matter pelletizer |
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| Publication Number | Publication Date |
|---|---|
| CN202410212U true CN202410212U (en) | 2012-09-05 |
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| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN2011204952091U Expired - Fee Related CN202410212U (en) | 2011-12-02 | 2011-12-02 | Oblique gas-liquid two-stage separator for exhaust system of waste industrial solid organic matter pelletizer |
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| Country | Link |
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| CN (1) | CN202410212U (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN103127739A (en) * | 2011-12-02 | 2013-06-05 | 洛阳骏腾能源科技有限公司 | Inclined type gas-liquid two-stage separator for waste industrial solid organic matter granulating machine exhaust system and separation method |
-
2011
- 2011-12-02 CN CN2011204952091U patent/CN202410212U/en not_active Expired - Fee Related
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN103127739A (en) * | 2011-12-02 | 2013-06-05 | 洛阳骏腾能源科技有限公司 | Inclined type gas-liquid two-stage separator for waste industrial solid organic matter granulating machine exhaust system and separation method |
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| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| C17 | Cessation of patent right | ||
| CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20120905 Termination date: 20121202 |