CN1415397A - Degasser - Google Patents
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- CN1415397A CN1415397A CN 02106817 CN02106817A CN1415397A CN 1415397 A CN1415397 A CN 1415397A CN 02106817 CN02106817 CN 02106817 CN 02106817 A CN02106817 A CN 02106817A CN 1415397 A CN1415397 A CN 1415397A
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Abstract
To provide a deaeration apparatus in which the deaeration operation and the exhaust operation in a gas-liquid separation tank are performed without using an expensive automatic three-way valve. A first check valve is provided in a first passage communicating with a liquid inlet and a second check valve is provided in a second passage connected to the liquid inlet in parallel to the 1st check valve. The tightly close gas-liquid separation tank for separating a gas from a liquid is provided in the first passage having the first check valve and a flow control valve communicating with the first check valve. One of suction and discharge ports of a bi-directional liquid circulation pump communicates with a liquid retaining part of the gas-liquid separation tank and another suction and discharge port communicates with the second check valve. A third check valve is provided in a third passage, through which another suction and discharge port of the circulation pump communicates with a liquid outlet. A stop valve for an exhaust gas is provided in a passage for the exhaust gas, through which a gas retaining part of the gas-liquid separation tank communicates with an exhaust gas outlet.
Description
Technical field
The present invention relates to a kind of degasser that makes gas-liquid separation.
Background technology
A kind of degasser with knockout drum is disclosed in the 2000-325703 patent gazette.
Above-mentioned existing degasser, as shown in Figure 6, pressure-regulating valve door 14 by open and close valve 12 and automatically three-dimensional valve 13 be connected under the liquid bath 11, the bottom of the hermetic type knockout drum 16 that the path 15 that pressure-regulating valve door 14 is housed and liquid are separated from the gas is connected.
This knockout drum 16 is provided with the liquid-level switch 17 of the liquid L of the 16a of liquid collecting portion of bottom in the monitoring jar and detects jar Pressure gauge 18 of internal pressure (vacuum pressure).
The 16a of liquid collecting portion of knockout drum 16 draws path 21, and the automatic shutter valve 22 on the path 21 links to each other with the suction inlet 23a of liquid circulation pump 23.The discharge opening 23b of this liquid circulation pump 23 is connected with the top of aforesaid liquid groove 11 by check valve 24, automatic three-dimensional valve 25, path 26 and switching valve 27.
Simultaneously, between the suction inlet 23a of above-mentioned automatic three-dimensional valve 13 and aforesaid liquid circulating pump 23, be provided with liquid circulation pump 23 directly in the pumping liquid groove 11 imbibition of liquid with path 31, and by knockout drum 16.
In addition, between aforementioned three-dimensional automatic valve 25 and aforementioned path 21, dispose the feed flow path 32 that the liquid of circulating pump 23 outputs is supplied to knockout drum 16.
And, between the top of aforementioned knockout drum 16 and aforementioned path 26, dispose exhaust channel 33, it is to be used for the liquid in the knockout drum 16 is returned in the liquid bath 11 from the top of knockout drum 16, the gas of the 16b of gas collection portion discharged use path, this path 33 is provided with automatic shutter valve 34.
Valve state during degassing running as shown in Figure 6, the suction inlet 23a of liquid circulation pump 23 is communicated with the bottom of liquid bath 11 through the 16a of liquid collecting portion, pressure-regulating valve door 14, automatic three-dimensional valve 13 and the controlled valve 12 of automatic switch valve 22, knockout drum 16, simultaneously, the discharge opening 23b of liquid circulation pump 23 is communicated with the top of liquid bath 11 through check valve 24, automatic three-dimensional valve 25, path 26 and controlled valve 27.At this moment, exhaust is closed because of automatic switch valve 34 with path 33 and is in closed condition.
Therefore, during degassing running, the suction decompression power of liquid circulation pump 23 acts on pressure-regulating valve door 14 by automatic switch valve 22 and hermetic type knockout drum 16, therefore is bubble in the molten gas from liquid that is stored in the liquid between pressure-regulating valve door 14 and knockout drum 16 and separates out.It is deaeration.
After this molten bubble of depositing gas enters knockout drum 16, separate release, do not enter liquid circulation pump 23 at the gas collection portion 16b place, top relative with the 16a of liquid collecting portion of bottom.Therefore, produce in the time of can not occurring the bubble that comes out from fluid separation applications by pump and make that the pump suction capactity descends, cavitation erosion and problems of dissolution again.
On the one hand, liquid level descends along with the gathering of the gas collection portion 16b place gas in the knockout drum 16, liquid-level switch 17 started when a large amount of alluvial gas made liquid level drop to the limit, its transducing signal automaticallyes switch aforementioned two automatic three-dimensional valves 13 and 25 respectively, and automatic switch valve 22 automatically switches to the path blockade state.Meanwhile automatic switch valve 34 automatically switches to the path opening state.
In other words, the suction inlet 23a of liquid circulation pump 23 by liquid suck path 31, three-dimensional valve 13 and controlled valve 12 are communicated with the bottom of liquid bath 11 automatically, the discharge opening 23b of liquid circulation pump 23 by check valve 24, automatic three-dimensional valve 25, feed flow path 32 be communicated with the bottom of knockout drum 16, the upper end of knockout drum 16 is communicated with the top of liquid bath 11 by exhaust usefulness path 33 and the controlled valve 27 that has the automatic shutter valve 34 that switches to the path opening state.
So, be used for the liquid circulation pump 23 shared with the degassing, by liquid suck path 31 and feed flow path 32 with the liquid discharge in the liquid bath 11 to knockout drum 16, so that the liquid level in the knockout drum 16 rises, this liquid is displaced in the liquid bath 11 by exhaust channel 33, emit thereby the gas that will be gathered in the 16b of gas collection portion of knockout drum 16 squeezes, make hermetic type knockout drum 16 turn back to the start of run state.
Conventional device is used 13,25 and two automatic switch valves 22,34 of two automatic three-dimensional valves, automatically three-dimensional valve 13 and 25 not only costs an arm and a leg, and automatically three-dimensional valve 13 and 25 and automatic shutter valve 22 and 34 are the valves that start by the signal of telecommunication, usage quantity multiple faults rate more is just high more, and therefore desirable way is to reduce valve quantity.
Summary of the invention
Use for reference above-mentioned situation, the object of the present invention is to provide the degasser that does not use expensive automatic three-dimensional valve promptly can realize degassing running and exhaust running by gas-liquid separation device.
Degasser characteristics of the present invention are, the type that two-way circulates liquid circulation pump, include, it when just changeing suction inlet, be that a side draught of discharge opening is told truth and is discharge opening when just changeing during counter-rotating, another side draught that during counter-rotating is suction inlet is told truth, with, be provided with to a side draught place of telling truth of liquid circulation pump in the liquid inlet first path and, be provided with to another side draught place of telling truth of liquid circulation pump in the liquid inlet alternate path and, in the suction of the opposite side of liquid circulation pump tell truth liquid outlet the 3rd path is set and be arranged on first path pressure regulating mechanism and, between another side draught of pressure regulating mechanism and liquid circulation pump is told truth, be provided with under decompression state, make gas-liquid separation tank arrangement that liquids and gases separate and, first, be respectively arranged with on second and third path only allow several check valve that liquid flows to the liquid outlet direction through liquid circulation pump by inlet and, openable exhaust controlled valve during from the gas collection portion exhaust of gas-liquid separation device.It is by the peculiar combination of two-way circulate type liquid circulation pump and a plurality of check valve, not only can omit expensive automatic three-dimensional valve, realize the exhaust running that outgases and turn round and make the gas discharge of assembling in the gas-liquid separation device by degassing running by gas-liquid separation device simultaneously.
The characteristics of degasser of the present invention are, first check valve that is provided with on first path that is communicated with the liquid inlet and, relative liquid inlet, with alternate path that first check valve is connected side by side be provided with second check valve and, the pressure regulating mechanism that is communicated with first check valve and, be connected with first path with first check valve and pressure regulating mechanism, make hermetic type knockout drum that liquids and gases separate and, the suction of liquid circulation pump one side of the type that two-way circulates is told truth and is communicated with the liquid collecting portion of knockout drum, the suction of opposite side is told truth and the second check valve connected sum, the suction that is communicated with the opposite side of liquid circulation pump tell truth and the 3rd path of liquid outlet in be provided with the 3rd check valve and, be communicated with the gas collection portion of knockout drum and the exhaust of air exit and be provided with the exhaust controlled valve with path.By the distinctive combination of two-way circulate type liquid circulation pump and first, second, third check valve, realized the exhaust running that need not expensive automatic three-dimensional valve also available original knockout drum outgases running and discharge by the gas that degassing running will be gathered in the knockout drum.
Be provided with in the knockout drum of degasser liquid level in surveying jar drop to decide the liquid-level switch of liquid level, liquid circulation pump be according to liquid-level switch detect the liquid level dropping signal, the side that is connected with knockout drum automatically switches to the automatic switchover pump of discharge opening by suction inlet, the controlled valve that exhaust is used is the automatic shutter valve that is automatically converted to the path opening state according to liquid-level switch detection liquid level dropping signal path by closed condition.It detects the liquid circulation pump of liquid level decline situation and the automatic switchover that controlled valve is used in exhaust by liquid-level switch, switching that running and exhaust turn round automatically can outgas, when omitting automatic three-dimensional valve, the quantity of automatic shutter valve is minimized simultaneously, thereby the fault rate that automatic switch valve is caused drops to bottom line.
Degasser possesses first path that links to each other with the liquid inlet and is provided with liquid with controlled valve and the pressure regulating mechanism that is connected with the liquid switch valve; Gas-liquid separation device comprises with pressure regulating mechanism and joining, with the gas removal in the liquid and make it agglomerateization degassing tank and, gas by the degassing tank agglomerateization is located away from the hermetic type knockout drum on the liquid level, and first path between degassing tank and the knockout drum is provided with first check valve.Distinctive combination by two-way circulate type liquid circulation pump and several check-valves, realization need not high price automatic three-dimensional valve, the degassing running of the efficient degassing of under the combination of degassing tank and knockout drum, carrying out and the exhaust running of discharging by the gas that degassing running is gathered in knockout drum.
Particularly, gas-liquid separation device have the degassing tank that removes gas in the liquid and make it agglomerateization and, will be in degassing tank the gas of agglomerateization be located away from knockout drum on the liquid, the gas that removes from liquid in degassing tank forms big air mass, after this air mass and liquid enter knockout drum simultaneously, air mass rises rapidly and efficiently isolates liquid surface in knockout drum, therefore not only can dwindle the diameter of knockout drum, but also can accelerate the interior flow velocity of knockout drum, improve degassing efficiency.
Degassing tank in the degasser is to be made of with packing material a degassing tank body and a jar interior promotion degassing of filling, pressure regulation effect by pressure regulating mechanism and the suction of liquid circulation pump make the liquid in the tank body that enters the degassing tank that has been depressurized contact with filler, on the filler surface gas are removed from liquid effectively.
Having a detection jar interior liquid level in the knockout drum of degasser descends in the liquid-level switch of deciding liquid level, liquid circulation pump is the detection liquid level dropping signal that sends according to liquid-level switch, automatically switch to the automatic switchover pump of exhaust end by the suction side with a side that is connected of knockout drum, to be the liquid level dropping signal path that sends according to liquid-level switch automatically switch to the automatic shutter valve of path blockade state by opening state to the controlled valve that liquid is used, and the controlled valve that exhaust is used is the automatic shutter valve that is automatically switched to the path opening state according to the liquid level dropping signal path that liquid-level switch sends by closed condition.According to the liquid level decline detection signal drives liquid circulation pump of liquid-level switch, liquid is used controlled valve with controlled valve and exhaust automatic switchover, can outgas the automatically switching of running and exhaust running, thus the while, it abolished the fault rate that automatic three-dimensional valve has reduced automatic valve.
Description of drawings
The conduit line map of Fig. 1 degasser example of the present invention.
Conduit line map when Fig. 2 degasser shown in Figure 1 switches to the exhaust running.
The conduit line map of another example of Fig. 3 degasser of the present invention.
Conduit line map when Fig. 4 degasser shown in Figure 3 switches to the exhaust running.
The sectional view of the degassing tank in Fig. 5 (a) degasser shown in Figure 3,
Fig. 5 (b) is filled in the Action Specification figure of the filler in the degassing tank.
The conduit line map of Fig. 6 prior art degasser.Symbol description
41 liquid inlets
43 first paths
44 first check valve
45 alternate paths
46 second check valve
47 flow control valves as the pressure regulating measure
48 knockout drums as gas-liquid separation device
48 gas-liquid separation devices
The 48a degassing tank
The 48b knockout drum
49 liquid controlled valves
51 liquid collecting portions
52 liquid-level switches
53 gas collection portions
The 55 type liquid circulation pumps that two-way circulate
The suction of 56 1 sides is told truth
The suction of 57 opposite sides is told truth
61 liquid outlets
63 the 3rd paths
64 the 3rd check valve
65 air exits
66 exhaust paths
67 exhaust controlled valves
71 jars of bodies
72 fillers
The specific embodiment
Below, reference is by example illustrated in figures 1 and 2, and the present invention will be described for another example shown in Fig. 3 ~ 5.
The example of Figure 1 and Figure 2 at first is described.
As shown in Figures 1 and 2, first path 43 that is communicated with the inlet valve 42 of liquid inlet 41 is provided with first check valve 44, simultaneously, 41 inlet valves 42 in the liquid inlet, the alternate path that is connected side by side with first check valve 44 is provided with second check valve 46.
Liquid collecting portion 51 places in these knockout drum 48 bottoms, be provided with liquid-level switch 52, in detecting jar by it liquid level drop to decide liquid level and detect a jar interior gas flow, simultaneously, gas collection portion 53 places on knockout drum 48 tops are provided with the pressure switch 54 of the band display of decompression state certain in detecting jar.
The liquid collecting portion 51 of knockout drum 48 and the suction of a side of the type water pumps 55 that two-way circulate such as for example turbulence pump are told truth and 56 are connected, and the suction of the opposite side of liquid circulation pump 55 is told truth 57 and is connected with second check valve 46 that is provided with in the alternate path.
With the suction of the opposite side of liquid circulation pump 55 tell truth 57 and the 3rd path 63 that is connected of the outlet valve 62 of liquid outlet 61 on, be provided with the 3rd check valve 64.
The exhaust that is communicated with the gas collection portion 53 and the air exit 65 of knockout drum 48 is provided with exhaust controlled valve 67 with on the path 66.This exhaust is the automatic switch valves that path automatically switched to the electromagnetic start formula of path opening state by closed condition according to the liquid level dropping signal that liquid-level switch 52 detects with controlled valve 67.
Secondly, the effect to the enforcement state of Figure 1 and Figure 2 is illustrated.
Fig. 1 shows the state of degassing running, closes and cut off exhaust with in the path 66 at the controlled valve 67 that exhaust is used, and liquid circulation pump 55 beginnings of the type that two-way circulates are just changeed, and knockout drum 48 sides become the suction side of pump.
When this degassing running, the suction decompression power of liquid circulation pump 55 acts on flow control valve 47 by knockout drum 48, therefore, be inhaled into the liquid of flow control valve 47 the molten gas of depositing through check valve 44 from the inlet valve 42 of liquid inlet 41 and be the bubble state separate out between flow control valve 47 and knockout drum 48, this promptly is so-called deaeration.
After this molten bubble of depositing gas enters knockout drum 48, separate release, do not enter liquid circulation pump 55 at bottom liquid collecting portion 51 relative gas collection portion 53 places, top.Therefore, can not take place that the bubble of separating out from liquid is low in the inlet capacity that has often by pump, cavitation erosion and problem such as dissolving again.
The liquid through deaeration that spues from liquid circulation pump 55 is cut off in second check valve 46, simultaneously, flows out from liquid outlet 61 dischargings via the 3rd check valve 64.
Simultaneously, along with the gathering of gas in knockout drum 48, liquid level descends, when liquid-level switch 52 detects condensed gas and forces liquid level to drop to critical liquid level, as shown in Figure 2, then running is switched to the exhaust operating condition of discharging gas in the knockout drum jar according to its signal immediately.
Exhaust running shown in Figure 2 according to above-mentioned switching signal, switches to the path opening state with opening and closing valve 67 paths by closed condition with above-mentioned exhaust automatically.Meanwhile, the type that two-way circulates liquid circulation pump 55 also automatically switches to counter-rotating by just changeing, and is connected side draught 56 exhaust ends that also automatically switched to pump by the suction side of pump of telling truth with the knockout drum 48 of liquid circulation pump 55 joins.
At this moment, the suction of liquid circulation pump 55 opposite sides 57 discharge openings by pump of telling truth switch to pump intake, therefore, second check valve 46 of the suction of liquid circulation pump 55 on alternate path 45, liquid is sucked in the liquid circulation pump 55 through second check valve 46 by the inlet valve 42 of liquid inlet 41, the liquid that spues through liquid circulation pump 55 is fed to knockout drum 48 bottoms, and the liquid level in the knockout drum 48 is risen.
Therefore, be gathered in the gas at gas collection portion 53 places of knockout drum 48,, be forced to outside exhaust channel 66 drain tanks through having the switching valve 67 that switches to the path opening state by upwards pushing of the liquid level that rises in the knockout drum 48.
Like this, utilize and shared liquid circulation pump 55 feed flow in knockout drum 48 of degassing running, make hermetic type knockout drum 48 return to the start of run state.
In a word, the degasser of the enforcement state of Figure 1 and Figure 2 comprises, one two-way circulation type liquid circulation pump 55, it when it is just changeing suction inlet, be that a side draught of discharge opening tells truth 56 and be discharge opening when just changeing during counter-rotating, during counter-rotating another side draught of suction inlet 57 Hes of telling truth, 41 to a side draught of liquid circulation pump 55 first path, 43 Hes that 56 places are provided with of telling truth in the liquid inlet, 41 to another side draught of liquid circulation pump 55 alternate path 45 Hes that 57 places are provided with of telling truth in the liquid inlet, in another side draught of liquid circulation pump 55 57 the 3rd path 63 Hes that are provided with to liquid outlet 61 places of telling truth, first path 43 is provided with flow control valve 47 Hes, flow control valve 47 a to side draught of liquid circulation pump 55 is told truth and is provided with between 56 under decompression state as knockout drum 48 Hes of gas-liquid separation device with gas and fluid separation applications, first, the second and the 3rd path 43,35, be respectively arranged with on 63, only allow liquid from the 41 a plurality of check valve 44 that flow to liquid outlet 61 directions through liquid circulation pump 55 that enter the mouth, 46,64 Hes, the exhaust of gas breakdown when the gas collection portion 53 of knockout drum 48 discharges is with opening and closing valve 67, by type liquid circulation pump 55 and a plurality of check valve 44 of two-way circulating, 46,64 distinctive combination, do not use expensive automatic three-dimensional valve, can by knockout drum 48 implement degassing operation and, the exhaust operation that the gases assembled in the knockout drum 48 is emitted by degassing running.
Secondly, Fig. 3 so that shown in Figure 5 be other example of the present invention.In addition, use same-sign, omit the explanation of this part at this in the part that the example of Figure 1 and Figure 2 is identical.
As shown in Figures 3 and 4, the type that two-way circulates liquid circulation pump 55 is provided with and is a side draught that suction inlet, counter-rotating the time be discharge opening 56 and that tell truth when just changeing, another side draught that is suction inlet when being discharge opening, counter-rotating when just changeing tells truth 57, liquid inlet 41 to the suction of a side of liquid circulation pump 55 is told truth and is provided with first path 43 between 56, liquid inlet 41 to the suction of the opposite side of liquid circulation pump 55 is told truth and is provided with alternate path 45 between 57, and the suction of the opposite side of liquid circulation pump 55 tells truth 57 to being provided with the 3rd path 63 between the liquid outlet.
This gas-liquid separation device 48, have be connected, remove the gas in the liquid with flow control valve 47 and make it agglomerateization degassing tank 48a and, make the gas of agglomerateization among the degassing tank 48a be located away from hermetic type knockout drum 48b on the liquid level, be provided with first check valve 44 in first path 43 between degassing tank 48a and the knockout drum 48b.
In first, second and third path 43,45,63, be respectively equipped with only allow liquid from the liquid inlet 41 check valve 44,46 and 64 that flow to liquid outlet 61 by liquid circulation pump 55, exhaust is provided with the exhaust usefulness controlled valve of opening 67 when the gas collection portion 53 of gas-liquid separation device 48 discharges gases with path 66.
In addition, liquid is the electromagnetic start formula automatic switch valves that the path blockade state automatically switched to the path opening state according to the liquid level dropping signal that liquid-level switch 52 detects with controlled valve 49.
Shown in Fig. 5 (a), degassing tank 48a is made of with filler 72 the jar body 71 and the promotions degassing that is filled in jar body 71.Filler 72 is the irregular charges with the lineament of metals such as stainless steel, titanium alloy, nickel making.
Simultaneously, rely on the pressurization of control valve 47 and the suction of liquid circulation pump 55, degassing tank 48a and knockout drum 48b are depressurized simultaneously, therefore under this decompression state, shown in Fig. 5 (b), the liquid 73 that enters in the degassing tank 48a body 71 contacts with charges 72, can make the gas of separating in the liquid 73 74 in the efficient degassing in filler 72 surfaces.
In addition, because the gas 74 that takes off from liquid 73 among the degassing tank 48a forms big gas agglomerate, and is located away from the liquid level rapidly, thereby can make the reduced of knockout drum 48b in knockout drum 48b.
Relative therewith, as not being set, degassing tank 48a only uses knockout drum 48b, the gas that produces in the knockout drum 48b under the decompression is micro air bubble, the separating rate that gas is located away from the liquid is slow, the rise speed of the separation on liquid level of the gas of generation slows down in the decompression knockout drum 48b down, and the flow velocity of the liquid that moves of must slowing down in jar just can make gas separate fully with liquid, so have to strengthen the slow down flow velocity of pot liquid of the diameter of knockout drum 48b.
Below, just Fig. 3 describes to the effect of example shown in Figure 5.
State for degassing running shown in Figure 3, liquid is opened with controlled valve 49 it is communicated with first path 43, and exhaust channel 66 is closed and cut off to exhaust with controlled valve 67, in this simultaneously, the type that two-way circulates liquid circulation pump 55 is just changeing, and makes knockout drum 48b side become the suction side of pump.
In this degassing running, suction decompression masterpiece is used for degassing tank 48a and the knockout drum 48b between the circulating pump 55 of the flow control valve 47 of control fluid flow and suction liquid, therefore, survival gas is bubble and is separated out (being deaeration) from the inlet valve 42 of liquid inlet 41 is inhaled into the liquid of degassing tank 48a via controlled valve 49 and flow control valve 47.
Enter the liquid 73 of degassing tank 48a and contacting of filler 72 by decompression, on filler 72 surfaces, gas 74 can be removed from liquid 73 effectively.The gas of being deviate from from liquid 73 in knockout drum 48a 74 is that bubble shape is separated out with air mass.
Above-mentioned bubble is in the state of sneaking among the liquid and enters knockout drum 48b via first check valve 44 1, will separatedly be released to the gas collection portion 53 on liquid collecting portion 51 tops, does not enter liquid circulation pump 55.Therefore, low, cavitation erosion of the inlet capacity that by pump the time, causes of the bubble that does not take place usually to separate out and problem such as dissolving again from liquid.
The liquid of deaeration that spues from liquid circulation pump 55 is discharged by liquid outlet 61 via the 3rd check valve 64 when being cut off by second check valve 46.
On the other hand, along with the gathering of gas in knockout drum 48b, liquid level descends, and liquid-level switch 52 sends signal when a large amount of air accumulations makes liquid level drop to the limit detecting, and makes knockout drum 48b shown in Figure 4 switch to the exhaust operating condition.
Exhaust running as shown in Figure 4, the liquid level decline detection signal that sends according to above-mentioned liquid-level switch 52, liquid automatically switches to the path blockade state with controlled valve 49 by the path opening state, and exhaust is changed to the path opening state with controlled valve 67 automatically by the path blockade state.Meanwhile, the type that two-way circulates liquid circulation pump 55 automatically switches to counter-rotating by just changeing, and the suction that is connected with the knockout drum 48 at liquid circulation pump 55 places is told truth and 56 automatically switched to the pump exhaust end by the pump suction side.
At this moment, another side draught of liquid circulation pump 55 is told truth and 57 is switched to Pump Suction Nozzle by the pump discharge opening, so second check valve 46 of suction in alternate path 45 of liquid circulation pump 55, liquid is inhaled in the liquid circulation pump 55 through second check valve 46 by the inlet valve 42 of liquid inlet 41, the liquid that spues from liquid circulation pump 55 enters the bottom of knockout drum 48b, and the liquid level in the knockout drum 48b is risen.
Therefore, be gathered in the gas of knockout drum 48b gas collection portion 53,, be forced to via the exhaust that has the controlled valve 67 that switches to opening state with outside path 66 drain tanks by upwards pushing of the liquid level that rises in the knockout drum 48b.
When this exhaust running, the suction pressure of liquid circulation pump 55 does not influence degassing tank 48a by the effect of controlled valve 49, and the pressure that spues of liquid circulation pump 55 does not influence degassing tank 48a by the effect of first check valve 44 yet.
And shared liquid circulation pump 55 feed flow in knockout drum 48b when utilizing with degassing running can make hermetic type knockout drum 48b return to the start of run state thus.
Like this, the two-way circulate specific combination of type liquid circulation pump 55 and a plurality of check valve 44,46 and 64 of employing, even need not expensive automatic three-dimensional valve, also can realize degassing tank 48a and knockout drum 48b efficient degassing running and, the exhaust running that the gas that utilizes degassing running to make to assemble in the knockout drum 48b is discharged.
Particularly, gas-liquid separation device 48 have the degassing tank 48a that removes the gas in the liquid and make it agglomerateization and, the gas of agglomerateization among the degassing tank 48a is located away from knockout drum 48b on the liquid level, the gas of deviating from from liquid in degassing tank 48a forms big air mass, after this air mass enters knockout drum 48b with liquid, air mass rises rapidly in knockout drum 48b, be located away from liquid level efficiently, therefore with do not add degassing tank 48a and compare, not only can dwindle the diameter of knockout drum 48b, can also accelerate the flow velocity in the knockout drum 48b, improve degassing efficiency.
Simultaneously, liquid level dropping signal according to the detection of liquid-level switch 52, liquid circulation pump 55, liquid automatically switch with controlled valve 67 with controlled valve 49 and exhaust, realized the automatic switchover between degassing running and exhaust running, and, can also reduce the fault rate of automatic valve owing to do not use automatic three-dimensional valve.
As described above, one example and another example, peculiar combination by two-way circulate type liquid circulation pump and a plurality of check valve, do not use expensive three-dimensional automatic valve, can realize relying on gas-liquid separation device degassing running and, will accumulate in the exhaust running that the gas in the knockout drum is discharged by degassing running.
The specific combination that the liquid circulation pump that dependence is two-way circulated and a plurality of check valve constitute, the degassing that can not use expensive automatic three-dimensional valve to carry out gas-liquid separation device turn round and will accumulate in the exhaust running that the gas in the knockout drum is discharged by degassing running.
By the peculiar combination of two-way circulate type liquid circulation pump and first, second and third check valve, need not expensive automatic three-dimensional valve reach with identical in the past knockout drum under degassing running and will accumulate in the exhaust running that the gas in the knockout drum is discharged by degassing running.
By liquid-level switch detection of liquid level decline situation, liquid circulation pump and the exhaust automatic switchover of controlled valve, the automatic switchover that running and exhaust turn round can outgas, this is external when having omitted automatic three-dimensional valve, the quantity of automatic switch valve has been reduced to bottom line, thereby the fault rate that the control automatic switch valve causes drops to bottom line.
The specific combination that constitutes by the liquid circulation pump that two-way circulates and a plurality of check valve, do not use expensive automatic three-dimensional valve, realize by gas-liquid separation device outgas efficiently running and, degassing running exhaust that the gas assembled in the gas-liquid separation device is discharged is turned round thus.
Particularly, gas-liquid separation device have remove gas in the liquid and the degassing tank that makes it to assemble and, be located away from knockout drum on the liquid level with accumulating in gas in the degassing tank, the gas that removes the liquid in degassing tank forms big agglomerate, after agglomerate that this is big and liquid enter knockout drum simultaneously, air mass in the knockout drum rises rapidly and efficiently separates from liquid level, therefore not only can dwindle the diameter of knockout drum, and can accelerate the interior flow rate of liquid of knockout drum, improve degassing efficiency.
By the pressurization of pressure regulating mechanism and the suction of liquid circulation pump the liquid in the post-decompression degassing tank is contacted with filler, can make the efficiently degassing in the gas from liquid on the filler surface.
Liquid circulation pump, liquid automatically switch according to the liquid level dropping signal that liquid-level switch sends with controlled valve with controlled valve and exhaust, the switching of degassing running and exhaust running is carried out automatically, and, owing to omitted automatic three-dimensional valve, can suppress the fault rate of automatic valve.
Claims (6)
1. a degasser is characterized in that,
The liquid circulation pump of the type that two-way circulates includes, when just changeing be suction inlet, counter-rotating the time be a side draught of discharge opening tell truth and when being discharge opening, counter-rotating when just changeing be another side draught of suction inlet tell truth and
Be provided with to the suction place of telling truth of liquid circulation pump one side in the liquid inlet first path and
Be provided with to the suction place of telling truth of the opposite side of liquid circulation pump in the liquid inlet alternate path and
In another side draught of liquid circulation pump tell truth to liquid outlet be provided with the 3rd path and
Be arranged on first path pressure control mechanism and
Between the suction of pressure control mechanism and liquid circulation pump one side is told truth, be provided with under reduced pressure make liquid gas-liquid separation device separated from the gas and
On first, second and third path, be respectively arranged with only allow several check valve that liquid flows to the liquid outlet direction through liquid circulation pump by inlet and
Openable exhaust is with opening and closing valve during the gas collection portion exhaust of gas-liquid separation device.
2. a degasser is characterized in that,
First path that links to each other with the liquid inlet be provided with first check valve and
Relative liquid inlet, with alternate path that first check valve is connected side by side be provided with second check valve and
The pressure control mechanism that links to each other with first check valve and
Be connected with first path with first check valve and pressure control mechanism, hermetic type knockout drum that liquid is separated from the gas and
The suction of the type that two-way circulates liquid circulation pump one side tell truth be connected with the liquid collecting portion of knockout drum, another side draught is told truth with second check valve be connected and
The suction that is communicated with the opposite side of liquid circulation pump is told truth and the 3rd path of liquid outlet be provided with the 3rd check valve and
Be communicated with the liquid collecting portion of knockout drum and the exhaust of air exit and be provided with exhaust with opening and closing valve with path.
3. degasser as claimed in claim 2 is characterized in that,
Be provided with in the knockout drum liquid level descends in detecting jar liquid-level switch and
Liquid circulation pump is the liquid level dropping signal that detects according to liquid-level switch, and a side that is connected with knockout drum is automatically converted to the automatic conversion pump of exhaust end by the suction side;
The switching valve that exhaust is used is the automatic conversion valve that is automatically converted to the path opening state according to the liquid level dropping signal path that liquid-level switch detects by closed condition.
4. degasser as claimed in claim 1 is characterized in that,
First path that links to each other with the liquid inlet be provided with liquid with open and close valve and
Open and close the pressure control mechanism that valve joins with liquid,
Gas-liquid separation device comprises
Link to each other with pressure control mechanism, with the gas removal in the liquid and make it agglomerateization degassing tank and
Be located away from the knockout drum of the hermetic type on the liquid by the gas of degassing tank agglomerateization,
First path between degassing tank and the knockout drum is provided with first check valve.
5. degasser as claimed in claim 4 is characterized in that,
Degassing tank be by the degassing tank body and
The promotion degassing of tank interior filling constitutes with filler.
6. as claim 4 or 5 described degassers, it is characterized in that,
Be provided with in the knockout drum and detect jar liquid-level switch that interior liquid level descends,
Liquid circulation pump is the liquid level dropping signal that sends according to liquid-level switch, and a side that is connected with knockout drum is automatically converted to the automatic conversion pump of exhaust end by the suction side,
To be the liquid level dropping signal path that sends according to liquid-level switch be automatically converted to the automatic shutter valve of path blockade state by opening state to the switching valve that liquid is used,
The switching valve that exhaust is used is the automatic shutter valve that is automatically converted to the path opening state according to the liquid level dropping signal path that liquid-level switch sends by closed condition.
Applications Claiming Priority (2)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP2001333354 | 2001-10-30 | ||
| JP2001333354A JP3682431B2 (en) | 2001-05-24 | 2001-10-30 | Deaerator |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| CN1415397A true CN1415397A (en) | 2003-05-07 |
| CN1183991C CN1183991C (en) | 2005-01-12 |
Family
ID=19148626
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN 02106817 Expired - Fee Related CN1183991C (en) | 2001-10-30 | 2002-03-04 | Degasser |
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| Country | Link |
|---|---|
| CN (1) | CN1183991C (en) |
Cited By (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN102895039A (en) * | 2012-05-08 | 2013-01-30 | 北京捷立德口腔医疗设备有限公司 | Oral vacuum continuous-suction double (multi)-tank-based automatically-switching liquid-gas separation control device |
| CN101990654B (en) * | 2008-04-08 | 2015-10-07 | 康明斯过滤Ip公司 | There is the inertial gas-liquid separator of valve and variable flow actuator |
| CN105592902A (en) * | 2013-09-30 | 2016-05-18 | 利乐拉瓦尔集团及财务有限公司 | Method and apparatus for liquid/solid separation such as dewatering particulate solids and agitation leaching |
| CN109496161A (en) * | 2016-08-08 | 2019-03-19 | 大阳日酸株式会社 | Gas-liquid separation device |
| CN110022958A (en) * | 2016-11-29 | 2019-07-16 | 田村稔 | The degasser that the gas componant for being dissolved in liquid is removed |
-
2002
- 2002-03-04 CN CN 02106817 patent/CN1183991C/en not_active Expired - Fee Related
Cited By (8)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN101990654B (en) * | 2008-04-08 | 2015-10-07 | 康明斯过滤Ip公司 | There is the inertial gas-liquid separator of valve and variable flow actuator |
| CN102895039A (en) * | 2012-05-08 | 2013-01-30 | 北京捷立德口腔医疗设备有限公司 | Oral vacuum continuous-suction double (multi)-tank-based automatically-switching liquid-gas separation control device |
| CN105592902A (en) * | 2013-09-30 | 2016-05-18 | 利乐拉瓦尔集团及财务有限公司 | Method and apparatus for liquid/solid separation such as dewatering particulate solids and agitation leaching |
| CN105592902B (en) * | 2013-09-30 | 2018-12-18 | 利乐拉瓦尔集团及财务有限公司 | Degassing system and method for degassing |
| CN109496161A (en) * | 2016-08-08 | 2019-03-19 | 大阳日酸株式会社 | Gas-liquid separation device |
| US11607627B2 (en) | 2016-08-08 | 2023-03-21 | Taiyo Nippon Sanso Corporation | Method for producing a gas |
| CN110022958A (en) * | 2016-11-29 | 2019-07-16 | 田村稔 | The degasser that the gas componant for being dissolved in liquid is removed |
| CN110022958B (en) * | 2016-11-29 | 2022-10-04 | 田村稔 | Degasser for removing gas components dissolved in liquid |
Also Published As
| Publication number | Publication date |
|---|---|
| CN1183991C (en) | 2005-01-12 |
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