CN104874198A - Condensable gaseous substance recycling method and condensable gaseous substance recycling system suitable for tail gas and exhaust gas - Google Patents
Condensable gaseous substance recycling method and condensable gaseous substance recycling system suitable for tail gas and exhaust gas Download PDFInfo
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- CN104874198A CN104874198A CN201510167919.4A CN201510167919A CN104874198A CN 104874198 A CN104874198 A CN 104874198A CN 201510167919 A CN201510167919 A CN 201510167919A CN 104874198 A CN104874198 A CN 104874198A
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Abstract
The invention discloses a condensable gaseous substance recycling method and a condensable gaseous substance recycling system suitable for tail gas and exhaust gas. According to the method, steam or other gaseous substances which are naturally separated from smoke/dust and are positioned above a discharging opening are introduced into a gas delivery pipe through a gas collecting hood positioned above industrial furnace/tower tail gas or smoke discharging opening, the steam or other gaseous substances coming from the gas delivery pipe are mixed with jet water or jet flows of other liquid flow through a liquid-gas mixer, the steam and other gaseous substances are converted into liquid water or other liquid flows to be recycled, and the liquid-gas mixer is used for sucking the steam or other gaseous substances in the gas delivery pipe by negative pressure formed by water or other liquid jet flows. The system comprises the gas collecting hood, the gas delivery pipe, the liquid-gas mixer and a pressurizing circulation pipeline. According to the invention, the structure is simple, the operation is convenient, and the handling capacity is high, and the method and system are not only suitable for the recycling of industrial dead steam or other gaseous substances, but also is particularly suitable for the recycling of steam in smoke of a power station boiler.
Description
Technical field
The present invention relates to a kind of be suitable for industrial furnace/tower class tail gas, the recovery method of steam (water vapour) or other gaseous materials and one are suitable for the recovery system of steam or other gaseous materials in the tail gas of industrial furnace/tower class, flue gas in flue gas.
Background technology
In the industrial furnace/tail gas of tower class and the flue gas of boiler, the source of steam or other gaseous materials has multiple, comprise moisture contained in raw material or other fluid liquids, reaction or the burn steam that produces or other gaseous materials and because entering tail gas in the processes such as wet type desulfurizing denitration, steam in flue gas or other gaseous materials etc., due to stove/tower class tail gas, steam in boiler smoke or the condensation of other gaseous materials bring very large harm by flue, therefore tail gas or flue-gas temperature is needed to control more than dew point corrosion, the whole moisture in tail gas or flue gas or other gaseous materials are together emitted with tail gas or flue gas from floss hole, steam contained in tail gas a large amount of thus or flue gas or other gaseous materials and heat energy are wasted, particularly for station boiler, because fuel quantity is large, and the wet method that adopts carries out desulfurization and denitration more at present, the quantity of steam discharged by flue gas form is very large.
Also lack the method being suitable for reclaiming steam or other gaseous materials in tail gas or flue gas at present, and before passing through discharged, on the ground steam or other gaseous materials cannot be separated from tail gas or flue gas, and the chimney of general industry stove/tower class exhaust emissions tower, station boiler is all very high, the steam adopting existing conventional method to arrange from tail gas or flue gas or other gaseous materials introduce ground installation and the cost carrying out being separated and reclaiming is very high, does not have feasibility economically.
Summary of the invention
The object of this invention is to provide a kind of be suitable for industrial furnace/tower class tail gas, in flue gas steam or other gaseous materials recovery method and a kind of apply the method can from the tail gas of industrial furnace/tower class, flue gas the device systems of recovered steam or other gaseous materials, to be adapted to the needs of recovered steam or other gaseous materials from tail gas or flue gas, avoid the waste of contained steam or other gaseous materials and energy in tail gas or flue gas.
The technical solution adopted in the present invention:
A kind of tail gas being suitable for industrial furnace/tower class, the recovery method of steam or other gaseous materials in flue gas, it is by being positioned at the gas skirt above floss hole, appendix is introduced with the steam of flue dust or dust natural separation or other gaseous materials (pending gas can be referred to as) by above floss hole, and mixed from the steam of appendix or other gaseous materials with water jets or other liquid jets by liquid air mixer, steam or other gaseous materials are converted to aqueous water or other fluid liquids reclaim, steam in the negative-pressure ward appendix that described liquid air mixer is formed with liquid jet or other gaseous materials, and according to this as the power by the steam above floss hole or other gaseous material suction gas skirts, described jet derives from the pressurized circulation system being provided with liquid pump, the endless form of the water of described pressurized circulation system or other fluid liquids (can be referred to as fluid liquid) is after water or other fluid liquids are discharged from liquid delivery side of pump, liquid air mixer is sent into and the jet of the water formed in liquid air mixer or other fluid liquids by supply pipe, enter the import of liquid pump through return duct after discharging from liquid air mixer, the unnecessary fluid liquid formed by steam or the conversion of other gaseous materials is drawn from return duct, the liquid obtained is reclaimed as steam or other gaseous materials.
Preferably, a described liquid air mixer high position is installed, described liquid pump low level is installed, described liquid pump adopts centrifugal pump, described supply pipe is also provided with or is not provided with pressure-setting valve, when being provided with pressure-setting valve, the water that described liquid pump outlet is discharged or other fluid liquids are introduced into pressure-setting valve, liquid air mixer is sent into through pressure-setting valve level pressure, the fluid flow of drawing from return duct is determined according to the water yield converted to by steam or other gaseous materials or fluid liquid flow, described supply pipe or return duct are provided with heat exchanger, the temperature of recirculated water or other fluid liquids is reduced by heat exchanger, described return duct is connected with delivery pipe, by described delivery pipe, the unnecessary fluid liquid flow formed by steam or the conversion of other gaseous materials is drawn from return duct, described delivery pipe is connected with or is not connected with hydrogenerator or is suitable for the turbo dynamo of other fluid liquids, when described discharge pipe is connected with hydrogenerator or be suitable for the turbo dynamo of other fluid liquids, described hydrogenerator or be suitable for other fluid liquids turbo dynamo low level install, the hydraulic pressure relying on potential energy to be formed drives hydrogenerator or turbo dynamo running, described liquid air mixer is provided with water under high pressure or other liquid pressure fluid inlets, steam or other gaseous material imports and the mixed outlet of liquid gas, primarily of interconnective power drive room and jet mixing room composition, described power drive room and jet mixing room are vertical or horizontal, described power drive room is positioned at top or the front end of described jet mixing room, be provided with in described liquid air mixer and described power drive room and jet mixing room are divided into two-part dividing plate, described dividing plate is provided with some playpipes, the entrance point of described playpipe is positioned at described power drive indoor, it is indoor that the port of export is positioned at described jet mixing, described jet mixing room is by from top to bottom or the suction chamber having from left to right to connect successively, reducing pipe, trunnion and increaser composition, top, described power drive room is provided with water under high pressure or other liquid pressure fluid inlets, top, described jet mixing room is provided with steam or other gaseous material suction inlets, the lower port of described increaser is the outlet for discharging mixing afterproduct, the axis of described power drive room and jet mixing room is positioned on the horizontal or vertical straight line of same, this horizontal or vertical straight line forms the main shaft of blender.
A kind of the method for applying can from the tail gas of industrial furnace/tower class, the recovery system of recovered steam or other gaseous materials in flue gas, it comprises gas skirt, appendix, liquid air mixer and pressurized circulation pipeline, described liquid air mixer is provided with water under high pressure or other liquid pressure fluids (can be referred to as pressure fluid) import, steam or other gaseous material imports and the mixed outlet of liquid gas (steam or other liquid, the mixed outlet of gas), described gas skirt is positioned at industrial furnace/tower class, above the floss hole of chimney etc., one end of described appendix connects the outlet of described gas skirt, the other end connects steam or other gaseous material imports of described liquid air mixer, described pressurized circulation pipeline comprises return duct, liquid pump and supply pipe, the two ends of described return duct connect the outlet of described liquid air mixer and the import of described liquid pump respectively, the two ends of described supply pipe connect water under high pressure or other liquid pressure fluid inlets of described liquid delivery side of pump and described liquid air mixer respectively, a described liquid air mixer high position is installed, usually can with the similar elevation of tail gas or soot emissions mouth, described liquid pump low level is installed, usually can arrange on the ground.
Preferably, described liquid pump adopts centrifugal pump, and described return duct is provided with reflux tube valve, and described supply pipe is provided with supply pipe control valve and supply pipe non-return valve, described pressurized circulation pipeline is also provided with following any one or multiple device:
(1) heat exchanger, its exothermic medium passage is serially connected on described supply pipe or on described return duct;
(2) heat abstractor, is serially connected on described supply pipe and/or return duct;
(3) pressure-setting valve, is serially connected on described supply pipe, and high-order installation;
(4) gathering-device, is serially connected on described recovery tube;
(5) outlet of centrifugal pump pressure instrumentation, is arranged on the described supply pipe that is positioned near described outlet of centrifugal pump.
Described return duct can also be connected with discharge pipe, described discharge pipe access gathering-device, heat-exchanger rig, purifier and reuse ducted any one, any two kinds, any three kinds or all.
Described liquid air mixer can primarily of interconnective power drive room and jet mixing room composition, described power drive room and jet mixing room are vertical or horizontal, described power drive room is positioned at top or the front end of described jet mixing room, the dividing plate described liquid air mixer being divided into top or power drive room, front end and bottom or jet mixing room, rear end is provided with in described liquid air mixer, described dividing plate is provided with some playpipes, the entrance point of described playpipe is positioned at described power drive indoor, it is indoor that the port of export is positioned at described jet mixing, described jet mixing room is by the suction chamber connected successively from top to bottom or from left to right, reducing pipe, trunnion and increaser composition, described top, power drive room or top are provided with water under high pressure or other liquid pressure fluid inlets, top, described jet mixing room is provided with steam or other gaseous material suction inlets, the lower port of described increaser is the outlet for discharging mixing afterproduct, the axis of described power drive room and jet mixing room is positioned on the horizontal or vertical straight line of same, this horizontal or vertical straight line forms the main shaft of blender.
Described dividing plate can in level or vertical discoid or in spherical crown shape, the centre of sphere that described spherical crown shape dividing plate is corresponding is positioned at below dividing plate or fluid levels flows on the described main shaft in front, the axis extended line that the axis of each described playpipe is all parallel to described main shaft or each described playpipe intersects on the main shaft in described trunnion, when described dividing plate is spherical crown shape and the axis extended line of each described playpipe intersects on the main shaft in described trunnion, the intersection point of the axis extended line of the centre of sphere that described spherical crown shape dividing plate is corresponding and each described playpipe is same point.
The inner side of described steam or other gaseous material suction inlets can be provided with oblique downwards or horizontal flow to deflector, described deflector is the axis cylindrical shape overlapping with described main shaft or the up big and down small or pre-large post-small cone barrel overlapping with described main shaft in axis, the port of export of each described playpipe is all positioned at described deflector, the diameter of described cylindrical shape deflector is less than the diameter on top, described jet mixing room, the top of described cone barrel deflector is connected with described dividing plate or is connected with the jet mixing chamber interior walls at below described dividing plate or rear, the rear end of described cone barrel deflector lower than or exceed described steam or other gaseous material suction inlets.
Described jet mixing room can be connected with for the gas delivery mask to jet mixing room delivering vapor or other gaseous materials, described gas delivery mask comprises outer wall and inwall, space between described gas delivery mask outer wall and inwall forms the medium channel in described gas delivery mask, the import of medium channel and the export mixes export and import of described gas delivery mask in described gas delivery mask, described gas delivery mask import forms steam or other gaseous material imports of described liquid air mixer, the outlet of described gas delivery mask is communicated with the steam of described jet mixing room or other gaseous material suction inlets, the import of described gas delivery mask is provided with the structure for connecting gas transmission pipe, the lower end of described gas delivery mask outer wall and inwall is all fixedly connected on the sidewall of described jet mixing room, realize the connection between described jet mixing room and gas delivery mask thus, gap between the lower end of described gas delivery mask outer wall and the lower end of described gas delivery mask inwall forms the outlet of described gas delivery mask, the steam of described jet mixing room or other gaseous material suction inlets are cylindrical opening on the sidewall of described jet mixing room or the multiple openings on being evenly distributed on the sidewall of described jet mixing room a face of cylinder, steam or other gaseous material suction inlets of described jet mixing room are positioned at described gas delivery mask, between the lower end of outer wall, in described gas delivery mask, the surface of revolution shape of main part all in the convex being axle with described main shaft of outer wall, the top seal of described inwall, the top of described outer wall is provided with the link upwards extended forming gas delivery mask import, top, described power drive room is positioned at described inwall, described gas delivery mask is provided with and runs through in it, the access opening closed of outer wall.
Steam on described jet mixing room or other gaseous material suction inlets can be one or more, when the quantity of described steam or other gaseous material suction inlets is one, described steam or other gaseous material suction inlets are provided with the appendix interface forming described steam or other gaseous material imports, when described steam or other gaseous material suction inlets are multiple, described multiple steam or other gaseous material suction inlets are symmetrically distributed on a face of cylinder on the sidewall of described jet mixing room, spacing between adjacent steam or other gaseous material suction inlets is all equal or all not identical, each described steam or other gaseous material suction inlets are connected to respective gas transmission arm, the axis of each described gas transmission arm lays respectively at same surface of revolution on the bus at position, respective place, the top of each described gas transmission arm converges at a common appendix connecting portion, described appendix connecting portion is directly over described power drive room or the rear end of direction of flow be provided with the appendix interface forming described steam or other gaseous material imports.
Beneficial effect of the present invention is: owing to have employed the top gas skirt being positioned at stove exhaust emissions tower or chimney, appendix can be introduced with the steam of flue dust or dust natural separation or other gaseous materials by above exhaust emissions tower or chimney, greatly simplifie being separated of steam in tail gas or flue gas or other gaseous materials and flue dust or dust thus, considerably reduce tail gas or flue dust or dust to recycle-water or the pollution of reclaiming other fluid liquids and circulation of fluid and the processing cost brought thus, due to the mode by aqueous vapor or the mixing of liquid gas, steam (comprising vaporous water) is converted to aqueous water or other gaseous materials are converted to fluid liquid, be very easy to storage thus, process, conveying and utilization, aqueous water steam in unserviceable tail gas or flue gas being become can be utilized or other gaseous materials become other fluid liquids that can be utilized, also the heat energy (particularly the latent heat of vaporization) contained by steam or other gaseous materials is transformed in mixed water or other fluid liquids simultaneously, improve water or other fluid liquid temperature, can be used to these heat energy by modes such as heat exchangers thus, in addition, this mixing conversion does not need harsh process conditions, the air be mixed into wherein can not affect the rate of recovery of steam or other gaseous materials substantially, due to liquid air mixer is arranged on a high position, under normal circumstances can with the floss hole similar elevation of tail gas or flue dust, not only shorten the fed distance of steam or other gaseous materials thus, decrease because of the relatively huge pipe-line system needed for delivering vapor or other gaseous materials, the water simultaneously formed or other fluid liquids are also in a high position, there is very large potential energy (position pressure head), the power-equipment such as water wheels or turbo dynamo can be promoted thus, to carry out the recycling of corresponding potential energy, in addition because the return duct of backwater or other fluid liquids can directly be connected with the import of centrifugal pump, form the return line of backwater or other fluid liquids closed, the position pressure head of aqueous vapor or liquid air mixer forms the inlet-pressure of centrifugal pump, centrifugal pump can be arranged on the power without the need to exorbitant expenditure on ground (comprising surface structures or structures etc.) thus, the negative-pressure ward steam utilizing water jet or other liquid jets to produce due to aqueous vapor or liquid air mixer or other gaseous materials, thus without the need to arranging blower fan, avoid because blower fan needs high-order installation and steam or other gaseous materials to problems such as the corrosion of blower fan, power consumption simultaneously also reduces relatively, due to corresponding aqueous vapor or liquid air mixer can be adopted, water under high pressure or all pressure of other liquid pressure fluids process in the upper space of power drive room at top, power drive room or top is entered from water under high pressure or other liquid pressure fluid inlets, substantially identical pressure is formed at the entrance point of each playpipe, ejection at a high speed after playpipe, at the indoor formation jet of jet mixing, the steam or other gaseous materials that connect steam or other gaseous material suction inlets are sucked, and constantly steam or other gaseous materials are entrainmented in jet in flow process, discharge heat energy and then be converted to aqueous water after steam contacts with water, discharge heat energy and be converted to other fluid liquids after other gaseous materials contact with other fluid liquids, become a part for fluid in jet, finally discharge in liquid form from the lower port of increaser, due to adding of steam or other gaseous materials, from increaser discharge fluid flow more than the fluid flow sent into from high-pressure water pipe, additional part is exactly reclaimed steam or other gaseous materials, the steam emitted originally utilizing thus becomes can by the water conveniently utilized, other gaseous materials emitted originally utilizing become can by other fluid liquids conveniently utilized, achieve the recovery of water from steam resource or the recovery of other gaseous material resources, because power drive room and jet mixing room all adopt vertical or horizontal, its power drive room and jet mixing room up and down or left and right distribution, axis is positioned on same horizontal or vertical straight line, if be arranged vertically, the potential energy of water or other fluid liquids can be made full use of, in the process of flows downward, its potential energy is constantly converted to kinetic energy, is conducive to significantly reducing power consumption and improving mixed effect, due to water under high pressure or other liquid pressure fluids enter power drive room after the cross-section of river enlarge markedly, play and well all press effect, make the pressure of each playpipe substantially identical, be conducive to the optimization realizing jet tissue, improve the suction capactity of gaseous fluid and entrainment ability, owing to have employed some playpipes, form the boundling shape jet of cylindricality or taper, make the suction capactity of steam or other gaseous materials and entrainment ability all much larger than the single jet of same flow, lessly in other words to conflict because boundling shape jet and the undergauge mode of reducing pipe are basically identical, be not only conducive to the speed continuing to increase jet, but also be conducive to the resistance that reduces because undergauge brings, be conducive to reducing power consumption, owing to being provided with the increaser after trunnion and trunnion, the mixing forming high strength at trunnion place is impacted and obtains sufficient heat exchange and condensation time at increaser, even if ensure that thus under the condition of rather harsh, also can realize the abundant mixing of steam and water and make steam all become liquid water, other gaseous materials and other fluid liquids fully being mixed and becomes other fluid liquids.
Structure of the present invention is simple, easy to operate, the gas flow that can process is large, not only be adapted to the recovery of industrial tail gas, exhaust steam, but also the flue gas in power station boiler that cannot realize under being adapted to prior art especially or the Steam Recovery in smelting, the water reclaimed directly or after certain purified treatment can be back to boiler desulfurization or other system, can not only be conducive to thus saving operating cost, but also the water resources consumption that can reduce boiler desulfurization system is in a large number even without the need to the consumption of consumption of new water or other other fluid liquids of production system.
Accompanying drawing explanation
Fig. 1 is the schematic diagram of a kind of steam of the present invention or other gaseous material recovery systems;
Fig. 2 is the structural representation of a kind of carbonated drink or the gas-liquid retracting device that the present invention relates to;
Fig. 3 is the schematic diagram of the another kind of steam of the present invention or other gaseous material recovery systems.
Detailed description of the invention
The tail gas being suitable for industrial furnace/tower class that the present invention relates to, in flue gas, the recovery method of vapor composition or other gaseous state condensable material matter compositions is by being positioned at the gas skirt above exhaust port or chimney, appendix is introduced with the steam of flue dust or dust natural separation or other gaseous materials by above it, and by liquid air mixer, the steam from appendix is mixed with water jets, or by the jet mixing of other gaseous materials and other fluid liquids, steam is converted to aqueous water, other gaseous materials are converted to other fluid liquids and reclaim, steam in the negative-pressure ward appendix that described liquid air mixer is formed with liquid jet (water jet or other liquid jets) or other gaseous materials, and according to this as the power by the steam above exhaust port or chimney or other gaseous material suction gas skirts, described jet derives from the pressurized circulation system being provided with liquid pump, described pressurized circulation system is used for carrying out pressurized circulation to water or other fluid liquids, the endless form of described water or other fluid liquids is after water or other fluid liquids are discharged from liquid delivery side of pump, liquid air mixer is sent into and the jet of the water jet formed in liquid air mixer or other fluid liquids by supply pipe, enter the import of liquid pump (preferred centrifugal pump) through return duct after discharging from liquid air mixer, the unnecessary water yield formed by steam conversion or other fluid liquids unnecessary formed by the conversion of other gaseous materials are drawn from return duct, the water obtained as Steam Recovery or other gaseous state condensable material matter reclaim other fluid liquids obtained.
Preferably, a described liquid air mixer high position is installed, and described liquid pump low level is installed, to simplify the unitary construction of system, save cost, facilitate operation and management, meanwhile, the water of steam formation or other fluid liquids of other gaseous materials formation have very high position pressure head.
Preferably, described liquid pump adopts the centrifugal pump being adapted to corresponding fluid liquid form.
Optionally, described supply pipe can be arranged voltage-stablizer (pressure-setting valve), also can not be provided with voltage-stablizer.When being provided with voltage-stablizer, the fluid (water or other fluid liquids) that described liquid pump outlet is discharged is introduced into voltage-stablizer, liquid air mixer is sent into through voltage-stablizer voltage stabilizing, ensure that liquid air mixer obtains stable water inlet or enters the pressure of other fluid liquids thus, be conducive to stable, meanwhile, be also conducive to the control carrying out centrifugal pump according to the data of voltage-stablizer, save power consumption.
Preferably, the fluid flow of drawing from return duct is determined according to the water yield converted to by steam or other gaseous materials or fluid liquid flow.
Preferably, described supply pipe or return duct are provided with heat exchanger, reduced the temperature of recirculated water or other liquid fluids, not only achieve the recycling of heat energy by heat exchanger, but also be conducive to the duty improving liquid air mixer, improve the suction capactity to steam or other gaseous materials.
Preferably, described return duct is connected with discharge pipe, by described delivery pipe, the unnecessary fluid liquid flow formed by steam or the conversion of other gaseous materials (the unnecessary water yield formed by steam conversion or other fluid liquids unnecessary formed by the conversion of other gaseous materials) is drawn from return duct, to realize stablizing and realizing the recovery to steam water or other gaseous materials of water or other fluid liquid pressurized circulation systems.
Optionally, described discharge pipe can be connected with hydrogenerator or be suitable for the turbo dynamo of other fluid liquids, also can not be connected with water wheels or turbo dynamo.When described discharge pipe is connected with hydrogenerator or be suitable for the turbo dynamo of other fluid liquids, described hydrogenerator or be suitable for other fluid liquids turbo dynamo low level install, the hydraulic pressure (position pressure head) relying on potential energy to be formed drives hydrogenerator or turbo dynamo running, recycles the potential energy in the water formed by steam conversion or other fluid liquids formed by the conversion of other gaseous materials thus.
Preferably, described liquid air mixer is provided with water under high pressure or other liquid pressure fluid inlets, steam or other gaseous material imports and the mixed outlet of liquid gas, primarily of interconnective power drive room and jet mixing room composition, described power drive room and jet mixing room are vertical or horizontal, described power drive room is positioned at top or the front end of described jet mixing room, be provided with in described liquid air mixer and described power drive room and jet mixing room are divided into two-part dividing plate, described dividing plate is provided with some playpipes, the entrance point of described playpipe is positioned at described power drive indoor, it is indoor that the port of export is positioned at described jet mixing, described jet mixing room is by from top to bottom or the suction chamber having from left to right to connect successively, reducing pipe, trunnion and increaser composition, top, described power drive room is provided with water under high pressure or other liquid pressure fluid inlets, top, described jet mixing room is provided with steam or other gaseous material suction inlets, the lower port of described increaser is the outlet for discharging mixing afterproduct, the axis of described power drive room and jet mixing room is positioned on the horizontal or vertical straight line of same, this horizontal or vertical straight line forms the main shaft of blender.
The various devices comprising liquid air mixer involved by method of the present invention all can adopt any one related device in following steam or other gaseous material recovery systems, method of the present invention can be realized by any one steam following or other gaseous material recovery systems, meanwhile, any one steam following or other gaseous material recovery systems also all can adopt any one method of the present invention.
See Fig. 1-3, the tail gas being suitable for industrial furnace/tower class that the present invention relates to, in flue gas, the recovery system of steam or other gaseous materials comprises gas skirt 410, appendix 420, liquid air mixer 100 and pressurized circulation pipeline, described liquid air mixer is provided with water under high pressure or other fluid liquid imports 121, steam or other gaseous material imports 112 and steam or the mixed outlet 170 of liquid gas, described gas skirt is positioned at the top of exhaust port or chimney 500, one end of described appendix connects the outlet of described gas skirt, the other end connects the steam of described liquid air mixer or the import of other gaseous materials, described pressurized circulation pipeline comprises return duct 210, centrifugal pump 220 and supply pipe 230, the two ends of described return duct connect the outlet (liquid of described liquid air mixer respectively, the mixed outlet of gas) and the import of described centrifugal pump, the two ends of described supply pipe connect water under high pressure or other fluid liquid imports of described centrifugal delivery side of pump and described liquid air mixer respectively, thus form circulation and the pressurization of water or other fluid liquids, rely on the pressure of centrifugal pump in liquid air mixer, form required jet.
Preferably, a described liquid air mixer high position is installed, usually can with flue dust or dust emission similar elevation, described centrifugal pump low level is installed, and usually can arrange on the ground.
Preferably, described water pump adopts centrifugal pump.
Preferably, described return duct is provided with reflux tube valve 211.
Preferably, described supply pipe is provided with supply pipe control valve 231.
Preferably, supply pipe non-return valve 232 on described supply pipe.
Preferably, described pressurized circulation pipeline is also provided with following any one or multiple device:
(1) heat exchanger, its exothermic medium passage is serially connected on described supply pipe or on described return duct;
(2) heat abstractor, such as cooling tower, be serially connected on described supply pipe and/or return duct;
(3) voltage-stablizer 240, preferred air-breathing pressure-setting valve or fire-fighting voltage-stablizer, be serially connected on described supply pipe, preferably high-order installation;
(4) liquid collector, such as collecting tank or liquid collecting tank, be serially connected on described recovery tube;
(5) outlet of centrifugal pump pressure instrumentation 233, be arranged on the described supply pipe that is positioned near described outlet of centrifugal pump, concrete installation site can be determined according to prior art, should guarantee outlet pressure centrifugal pump being detected in the error range allowed exactly.
Preferably, described return duct is also connected with discharge pipe 310, so that other fluid liquids water yield increased because of steam conversion or the conversion of other gaseous materials increased are drawn, to recycle.
Preferably, described discharge pipe access set liquid device 320, heat-exchanger rig 340, purifier and reuse ducted any one, any two kinds, any three kinds or all, when described discharge pipe accesses multiple device, can connect to device corresponding separately respectively by the connecting branch 330 of each device, each connecting branch can be provided with respective by-pass valve control 321,341.
Discharge pipe can be connected the exothermic medium import of heat exchanger by corresponding connecting branch, tail gas or flue gas are introduced the heat-absorbing medium interface of heat exchanger by corresponding pipeline, the outlet of the exothermic medium of heat exchanger is connected corresponding reuse pipeline to be processed and/or to utilize, the outlet of the heat-absorbing medium of heat exchanger is accessed exhaust emissions tower or stove chimney by connection passage 350, improve the temperature of tail gas or flue gas thus, and then improve the lifting ability of tail gas or flue gas.
The liquid air mixer 100 that the present invention relates to is primarily of interconnective power drive room 120 and jet mixing room composition, described power drive room and jet mixing room are vertical or horizontal, described power drive room is positioned at top or the left and right of described jet mixing room, the dividing plate 131 of jet mixing room liquid air mixer being divided into upper or anterior power drive room and lower or rear portion is provided with in described liquid air mixer, described dividing plate is provided with some playpipes 132, such as can fix welding or from upper, below clamp nut is fastening, the entrance point of described playpipe is positioned at described power drive indoor, it is indoor that the port of export is positioned at described jet mixing.
Preferably, the pattern of each playpipe is preferably the form of basic indiffusion or less diffusion, to make these little jet beams 141 accumulate the diminishing taper large stream in water cross section, to be applicable to be positioned at below described jet mixing room or the change of rear reducing pipe caliber, and, test display, under the occasion that the present invention adapts to, the diffusion of jet crosses the soakage that senior general obviously reduces steam or other gaseous materials.
Such as, preferably, the pore of described playpipe (or it ejects fluid section) is isometrical circular hole, port of export end face is that (namely its port of export end face and the intersection of the arbitrary plane crossing playpipe axis are that middle part (refers to the axis direction of playpipe here) vertically to the arc of injection direction projection for the arc surfaced of center projections, the arc of this projection is preferably semicircle or half elliptic, the little jet beam that the playpipe of this structure ejects is for a fluid stream that the port of export (nozzle) of other shapes sprays, diffusion obviously reduces, can produce in longer path thus and better entrainment effect, and be obviously conducive to the resistance reducing reducing pipe.The playpipe of some this structures is relied on to form boundling shape jet tissue, the steam that can suck or the flow of other gaseous materials adopt the equipment of jet suction apparently higher than Venturi tube and other, allow to be inhaled into rate-of flow to change in a wider context, in addition, adjusted design disposal ability can also be carried out by parameters such as the playpipe of selection suitable number and the power drive pipe calibers matched, in the steam of the flue gas etc. of existing chemical plant installations emission or the industrial furnace tail gas such as metallurgical or boiler of power plant or the discharge size range of tail gas or flue gas, when not changing playpipe size and other relative configurations, disposal ability is directly proportional substantially to the quantity of playpipe.
Described jet mixing pipe by from up to down or from left to right or the reducing pipe 140, trunnion 150 and the increaser 160 that connect successively such as right-to-left form, be similar to Venturi tube structure, but suction inlet is not set at trunnion place, but steam or other gaseous material suction inlets are set on top, jet mixing room or front end, the steam of suction and water jets or other gaseous materials and other fluid liquids are together sent into jet mixing pipe (also often having had mixing to a certain degree before entering jet mixing pipe).Overcome the defect that Venturi tube soakage is little thus, make treating capacity by selecting the power drive pipe caliber, playpipe quantity and other design parameters that adapt to, the processing requirements of the chemical plant installations of the existing any specification of China, industrial furnace, coal burning power boiler etc. can be met, on the other hand, because jet water and steam or other fluid liquids of jet together enter jet mixing pipe with other gaseous materials, just mixing from reducing pipe, substantially prolongs mixed path thus, the reducing pipe that originally there is not mixing in Venturi tube is made to have possessed immixture, because little jet beams some in reducing pipe exist certain impact and collision in the process flowed and spread, also because the caliber of reducing pipe reduces gradually, velocity of medium is accelerated gradually, make reducing pipe can have very strong immixture, make the abundant mixing that water and steam or other fluid liquids and other gaseous materials just realize or substantially achieve on material in trunnion, significantly can shorten the length of increaser thus, reduce volume and save manufacturing cost.
Described water under high pressure or other fluid liquid imports 121 of high pressure are arranged on described top, power drive room or top.Preferably, the chamber (inner space) on top, described power drive room is at the caliber that obviously should be greater than its water under high pressure connected or other liquid fluid duct of high pressure perpendicular to the size in water (flow) direction, to obtain enough all pressures effects, therefore the high pressure liquid fluid of power drive room is entered after all pressures of suitable degree, make each playpipe under identical or substantially identical pressure, eject substantially identical jet (little jet beam can be called) from the port of export.
Preferably, top, described power drive room is provided with the Pressure gauge for gathering its internal pressure or is provided with the interface 180 for setting pressure table.
Preferably, described high pressure liquid fluid import is preferably not less than 2/3 height on top, described power drive room at the height on top, described power drive room, described high pressure liquid fluid import can be opened on the sidewall of described power drive room, also the top of described power drive room can be opened in, and on the upper surface that the entrance point of described playpipe can be arranged on described dividing plate or be arranged on top, power drive room and it is not highly preferably higher than 1/2 height on top, described power drive room, to optimize current tissue, obtain good all pressures effect.
Preferably, top, described jet mixing room is provided with steam or other gaseous material suction inlets, make thus steam and water mix or steam from top, jet mixing room of gaseous state and other fluid liquids or other gaseous material suction inlet places, effectively extend the path of steam and water or gaseous state and the mixing of other fluid liquids, for Venturi tube, be conducive to significantly reducing axial length, particularly, the little jet beam of the taper boundling shape that some playpipes can be utilized to be formed, significantly increase the inlet capacity to steam or other gaseous materials, and the chemical plant installations related in practice, industrial furnace, in boiler of power plant flue gas steam or other gaseous material discharge capacitys scope in, can by changing the quantity of playpipe and the size of other parts, meet the recovery of steam under any discharge capacity or other gaseous materials.
Preferably, the lower port of described increaser is the outlet 170 for discharging the rear medium of mixing, is beneficial to reduce resistance.Can arrange in the lower end of described increaser and be used for pipeline coupling flange, or be arranged through connecting pipe that is isometrical or reducing, to connect with discharge pipe.
Preferably, the axis of described power drive room and jet mixing room is positioned on the horizontal or vertical straight line of same, and this horizontal or vertical straight line forms the main shaft of blender.Thus not only attractive in appearance, be convenient to manufacture, but also be conducive to reduce resistance.
Optionally, described dividing plate is the discoid of level, and can be also spherical crown shape, the centre of sphere that described spherical crown shape dividing plate is corresponding be positioned on the described main shaft below dividing plate, and namely middle part raises up.
Preferably, each described playpipe structure identical (comprising shape and size etc.), to make the speed of each playpipe ejection jet, flow and a fluid stream shape all substantially equal with size.
Optionally, the axis of each described playpipe is all parallel to described main shaft, or, the axis extended line of each described playpipe intersect at be positioned at below dividing plate or on right and left described main shaft a bit, this intersection point is preferably placed in described trunnion.Thus, the some little jet beam sprayed by each playpipe forms the boundling shape of uniform cylindricality or taper, and accumulates a large stream gradually, can increase significantly and also reduce resistance significantly to the soakage of steam or other gaseous materials.
Preferably, when described dividing plate be spherical crown shape and the axis extended line of each described playpipe intersect at be positioned at below dividing plate or front described main shaft on some time, the intersection point of the axis extended line of the centre of sphere that described spherical crown shape dividing plate is corresponding and each described playpipe is same point.
Preferably, the inner side of described steam or other gaseous material suction inlets is provided with deflector 133 downwards oblique or to the left or to the right, impact with the steam or other gaseous material stream of avoiding entering top, jet mixing room or front portion and destroy the due fluidised form tissue of jet, affect the suction capactity of steam or other gaseous materials and mixed effect and increase SR.Described deflector makes to enter the steam on top, jet mixing room or other gaseous materials flow to lower curved, can reduce the impact to the jet tissue of water or other fluid liquids and destruction thus.
Preferably, described deflector is the axis cylindrical shape overlapping with described main shaft or the up big and down small or pre-large post-small cone barrel (the side view of frustum of a cone or inverted round stage) overlapping with described main shaft in axis.
Preferably, the lower end of each described playpipe is all positioned at described deflector, the diameter of described cylindrical shape deflector is less than the diameter on top, described jet mixing room, the top of described cone barrel deflector is connected with described dividing plate or is connected with the jet mixing chamber interior walls below described dividing plate, the lower end of described cone barrel deflector or rear end lower than or be longer than the suction inlet of described steam or other gaseous materials, to obtain good water conservancy diversion effect.
As one preferred embodiment, by the mode that arranges gas delivery mask 110, the steam obtained or other gaseous materials can be introduced the suction inlet of steam or other gaseous materials.Be specially:
Preferably, described jet mixing room is connected with for the gas delivery mask to jet mixing room delivering vapor, described gas delivery mask is provided with export and import, the outlet of described gas delivery mask is communicated with the steam of described jet mixing room or other gaseous material suction inlets, the steam obtained or other gaseous materials to be introduced by gas delivery mask steam or other gaseous material suction inlets of jet mixing room, the import of described gas delivery mask can be provided with the appendix interface (such as arranging adpting flange) for connecting gas transmission pipe, also the other forms of structure that can be used in connecting gas transmission pipe can be provided with.
Preferably, described gas delivery mask comprises outer wall and inwall, space 111 between described gas delivery mask outer wall and inwall forms the medium channel in described gas delivery mask, the import of the medium channel in described gas delivery mask and the export mixes export and import of described gas delivery mask, described gas delivery mask import forms the steam of described liquid air mixer or the import of other gaseous materials, the lower end of described gas delivery mask outer wall and inwall is all fixedly connected on the sidewall of described jet mixing room, realizes the connection between described jet mixing room and gas delivery mask thus.
Preferably, gap between the lower end of described gas delivery mask outer wall and the lower end of described gas delivery mask inwall forms the outlet of described gas delivery mask, in this case, the steam of described jet mixing room or other gaseous material suction inlets are preferably the cylindrical opening on the sidewall of described jet mixing room or are evenly distributed on the multiple openings on a face of cylinder on the sidewall of described jet mixing room, and the steam of described jet mixing room or other gaseous material suction inlets are between the lower end of the inside and outside wall of described gas delivery mask.Such as, the jet mixing room relating to steam or other gaseous material suction inlets can be made, lower two-section, leave the spacing that forms described cylindrical steam or other gaseous material suction inlets between two-section and arrange for two-section being connected into an overall bracing frame, support frame as described above can be along sidewall place, described jet mixing room be circumferentially uniformly distributed and on, lower two ends connect on described jet mixing room respectively to be cut and some connecting rods of lower section, not only aperture area is large for the steam formed thus or other gaseous material suction inlets, cloth vapour is even, and manufacture and install also simple and convenient.
Preferably, in described gas delivery mask, the surface of revolution shape of main part all in the convex being axle with described main shaft of outer wall, the top seal of described inwall, the top of described outer wall is provided with the link upwards extended, the open top of this link is exactly the import of described gas delivery mask, the namely steam of described liquid air mixer or other gaseous material imports 112, top, described power drive room is positioned at described inwall, described gas delivery mask is provided with and runs through in it, (namely the hole wall of access opening is by gas delivery mask for the access opening closed of outer wall, gap between outer wall closes, in order to avoid steam in gas delivery mask or other gaseous materials leak from access opening).For ease of manufacturing, on the inside and outside wall of gas delivery mask after perforate, the short tube two ends difference seal welding of access opening hole wall can will be formed on the edge of opening of the inside and outside wall of gas delivery mask.Water under high pressure or other fluid liquid pipes of high pressure can be passed this access opening thus, also water under high pressure or other fluid liquid pipes of high pressure can be connected to form access opening hole wall short tube on, be directly used as water under high pressure through gas delivery mask or other fluid liquid pipes of high pressure with this short tube.
As another preferred embodiment, can not gas delivery mask be set, and otherwise the steam obtained or other gaseous materials be introduced steam or other gaseous material suction inlets.Be specially:
Preferably, the steam on described jet mixing room or other gaseous material suction inlets are one or more.When the quantity of described steam or other gaseous material suction inlets is one, described steam or other gaseous material suction inlets are provided with the appendix interface (such as arranging adpting flange) forming described steam or other gaseous material imports, when described steam or other gaseous material suction inlets are multiple, described multiple steam or other gaseous material suction inlets are symmetrically distributed on a face of cylinder on the sidewall of described jet mixing room, spacing between adjacent steam or other gaseous material suction inlets is all equal or all not identical, each described steam or other gaseous material suction inlets are connected to respective gas transmission arm, the top of each described gas transmission arm converges at a common appendix connecting portion, described appendix connecting portion is directly over described power drive pipe and be provided with the appendix interface (such as arranging adpting flange) forming described steam or other gaseous material imports.
Preferably, the axis of each described gas transmission arm lays respectively at same surface of revolution on the bus at position, respective place, is conducive to making the resistance of each gas transmission arm to reach the resistance of minimum and each gas transmission arm thus identical.
Connecting alleged by the present invention between device with pipeline is the connected mode that the medium stream of instigating this pipeline to transmit all flows through this device.Such as, by valve installation on pipeline, and for example, water inlet or the pipe outlet of other fluid approach axis are arranged on the top of collecting tank, make to flow into collecting tank into the water of the pipeline of water or other fluid liquid approach axis or other fluid liquids, the pipeline that direction is flowed out in water outlet or other fluid liquids is connected in the outlet of collecting tank, makes other fluid liquids of the water outlet of collecting tank enter the pipeline in water outlet or other fluid liquids outflow direction.
Except illustrating or clearly having except other different implications, the axis that this description relates to is the direction along main shaft.
Except illustrating or clearly having except other different implications, axis alleged by this description is identical with the implication of axis extended line, all represents the straight line at axis place or the straight-line segment of suitable length.
Except illustrating or clearly have except other different implications, the relative position relation of "left", "right" alleged by the present invention only on expression levels direction, be not used in right position when limiting actual use.
Except illustrating or clearly having except other different implications, main shaft alleged by the present invention comprises the main shaft being positioned at liquid air mixer and the main shaft (or claiming extended line of main shaft) be positioned at outside liquid air mixer.
Each optimization technique means disclosed by the invention, unless otherwise indicated and optimization technique means be outside the further restriction of another technological means, all can be combined, form some different technical schemes.
Claims (10)
1. one kind is suitable for the condensated gas state material recovery method of tail gas and flue gas, it is by being positioned at the gas skirt above floss hole, appendix is introduced with the steam of flue dust or dust natural separation or other gaseous materials by above floss hole, and mixed from the steam of appendix or other gaseous materials with water jets or other liquid jets by liquid air mixer, steam or other gaseous materials are converted to aqueous water or other fluid liquids reclaim, steam in the negative-pressure ward appendix that described liquid air mixer is formed with liquid jet or other gaseous materials, and according to this as the power by the steam above floss hole or other gaseous material suction gas skirts, described jet derives from the pressurized circulation system being provided with liquid pump, the water of described pressurized circulation system or the endless form of other fluid liquids are after water or other fluid liquids are discharged from liquid delivery side of pump, liquid air mixer is sent into and the jet of the water formed in liquid air mixer or other fluid liquids by supply pipe, enter the import of liquid pump through return duct after discharging from liquid air mixer, the unnecessary fluid liquid formed by steam or the conversion of other gaseous materials is drawn from return duct, the liquid obtained is reclaimed as steam or other gaseous materials.
2. condensated gas state material recovery method as claimed in claim 1, it is characterized in that a described liquid air mixer high position is installed, described liquid pump low level is installed, described liquid pump adopts centrifugal pump, described supply pipe is also provided with or is not provided with pressure-setting valve, when being provided with pressure-setting valve, the water that described liquid pump outlet is discharged or other fluid liquids are introduced into pressure-setting valve, liquid air mixer is sent into through pressure-setting valve level pressure, the fluid flow of drawing from return duct is determined according to the water yield converted to by steam or other gaseous materials or fluid liquid flow, described supply pipe or return duct are provided with heat exchanger, the temperature of recirculated water or other fluid liquids is reduced by heat exchanger, described return duct is connected with delivery pipe, by described delivery pipe, the unnecessary fluid liquid flow formed by steam or the conversion of other gaseous materials is drawn from return duct, described delivery pipe is connected with or is not connected with hydrogenerator or is suitable for the turbo dynamo of other fluid liquids, when described discharge pipe is connected with hydrogenerator or be suitable for the turbo dynamo of other fluid liquids, described hydrogenerator or be suitable for other fluid liquids turbo dynamo low level install, the hydraulic pressure relying on potential energy to be formed drives hydrogenerator or turbo dynamo running, described liquid air mixer is provided with water under high pressure or other liquid pressure fluid inlets, steam or other gaseous material imports and the mixed outlet of liquid gas, primarily of interconnective power drive room and jet mixing room composition, described power drive room and jet mixing room are vertical or horizontal, described power drive room is positioned at top or the front end of described jet mixing room, be provided with in described liquid air mixer and described power drive room and jet mixing room are divided into two-part dividing plate, described dividing plate is provided with some playpipes, the entrance point of described playpipe is positioned at described power drive indoor, it is indoor that the port of export is positioned at described jet mixing, described jet mixing room is by from top to bottom or the suction chamber having from left to right to connect successively, reducing pipe, trunnion and increaser composition, top, described power drive room is provided with water under high pressure or other liquid pressure fluid inlets, top, described jet mixing room is provided with steam or other gaseous material suction inlets, the lower port of described increaser is the outlet for discharging mixing afterproduct, the axis of described power drive room and jet mixing room is positioned on the horizontal or vertical straight line of same, this horizontal or vertical straight line forms the main shaft of blender.
3. one kind is suitable for the condensated gas state material recovery system of tail gas and flue gas, it is characterized in that comprising gas skirt, appendix, liquid air mixer and pressurized circulation pipeline, described liquid air mixer is provided with water under high pressure or other liquid pressure fluid inlets, steam or other gaseous material imports and the mixed outlet of liquid gas, described gas skirt is positioned at industrial furnace/tower class, above the floss hole of chimney etc., one end of described appendix connects the outlet of described gas skirt, the other end connects steam or other gaseous material imports of described liquid air mixer, described pressurized circulation pipeline comprises return duct, liquid pump and supply pipe, the two ends of described return duct connect the outlet of described liquid air mixer and the import of described liquid pump respectively, the two ends of described supply pipe connect water under high pressure or other liquid pressure fluid inlets of described liquid delivery side of pump and described liquid air mixer respectively, a described liquid air mixer high position is installed, described liquid pump low level is installed.
4. condensated gas state material recovery system as claimed in claim 3, it is characterized in that described liquid pump adopts centrifugal pump, described return duct is provided with reflux tube valve, described supply pipe is provided with supply pipe control valve and supply pipe non-return valve, described pressurized circulation pipeline is also provided with following any one or multiple device:
(1) heat exchanger, its exothermic medium passage is serially connected on described supply pipe or on described return duct;
(2) heat abstractor, is serially connected on described supply pipe and/or return duct;
(3) pressure-setting valve, is serially connected on described supply pipe, and high-order installation;
(4) gathering-device, is serially connected on described recovery tube;
(5) outlet of centrifugal pump pressure instrumentation, is arranged on the described supply pipe that is positioned near described outlet of centrifugal pump.
5. condensated gas state material recovery system as claimed in claim 4, it is characterized in that described return duct is also connected with discharge pipe, described discharge pipe access gathering-device, heat-exchanger rig, purifier and reuse ducted any one, any two kinds, any three kinds or all.
6. as claim 3, condensated gas state material recovery system described in 4 or 5, it is characterized in that described liquid air mixer is primarily of interconnective power drive room and jet mixing room composition, described power drive room and jet mixing room are vertical or horizontal, described power drive room is positioned at top or the front end of described jet mixing room, the dividing plate described liquid air mixer being divided into top or power drive room, front end and bottom or jet mixing room, rear end is provided with in described liquid air mixer, described dividing plate is provided with some playpipes, the entrance point of described playpipe is positioned at described power drive indoor, it is indoor that the port of export is positioned at described jet mixing, described jet mixing room is by the suction chamber connected successively from top to bottom or from left to right, reducing pipe, trunnion and increaser composition, described top, power drive room or top are provided with water under high pressure or other liquid pressure fluid inlets, top, described jet mixing room is provided with steam or other gaseous material suction inlets, the lower port of described increaser is the outlet for discharging mixing afterproduct, the axis of described power drive room and jet mixing room is positioned on the horizontal or vertical straight line of same, this horizontal or vertical straight line forms the main shaft of blender.
7. condensated gas state material recovery system as claimed in claim 6, it is characterized in that described dividing plate is level or vertical discoid or in spherical crown shape, the centre of sphere that described spherical crown shape dividing plate is corresponding is positioned at below dividing plate or fluid levels flows on the described main shaft in front, the axis extended line that the axis of each described playpipe is all parallel to described main shaft or each described playpipe intersects on the main shaft in described trunnion, when described dividing plate is spherical crown shape and the axis extended line of each described playpipe intersects on the main shaft in described trunnion, the intersection point of the axis extended line of the centre of sphere that described spherical crown shape dividing plate is corresponding and each described playpipe is same point.
8. condensated gas state material recovery system as claimed in claim 7, it is characterized in that the inner side of described steam or other gaseous material suction inlets be provided with oblique downwards or horizontal flow to deflector, described deflector is the axis cylindrical shape overlapping with described main shaft or the up big and down small or pre-large post-small cone barrel overlapping with described main shaft in axis, the port of export of each described playpipe is all positioned at described deflector, the diameter of described cylindrical shape deflector is less than the diameter on top, described jet mixing room, the top of described cone barrel deflector is connected with described dividing plate or is connected with the jet mixing chamber interior walls at below described dividing plate or rear, the rear end of described cone barrel deflector lower than or exceed described steam or other gaseous material suction inlets.
9. condensated gas state material recovery system as claimed in claim 8, it is characterized in that described jet mixing room is connected with for the gas delivery mask to jet mixing room delivering vapor or other gaseous materials, described gas delivery mask comprises outer wall and inwall, space between described gas delivery mask outer wall and inwall forms the medium channel in described gas delivery mask, the import of medium channel and the export mixes export and import of described gas delivery mask in described gas delivery mask, described gas delivery mask import forms steam or other gaseous material imports of described liquid air mixer, the outlet of described gas delivery mask is communicated with the steam of described jet mixing room or other gaseous material suction inlets, the import of described gas delivery mask is provided with the structure for connecting gas transmission pipe, the lower end of described gas delivery mask outer wall and inwall is all fixedly connected on the sidewall of described jet mixing room, realize the connection between described jet mixing room and gas delivery mask thus, gap between the lower end of described gas delivery mask outer wall and the lower end of described gas delivery mask inwall forms the outlet of described gas delivery mask, the steam of described jet mixing room or other gaseous material suction inlets are cylindrical opening on the sidewall of described jet mixing room or the multiple openings on being evenly distributed on the sidewall of described jet mixing room a face of cylinder, steam or other gaseous material suction inlets of described jet mixing room are positioned at described gas delivery mask, between the lower end of outer wall, in described gas delivery mask, the surface of revolution shape of main part all in the convex being axle with described main shaft of outer wall, the top seal of described inwall, the top of described outer wall is provided with the link upwards extended forming gas delivery mask import, top, described power drive room is positioned at described inwall, described gas delivery mask is provided with and runs through in it, the access opening closed of outer wall.
10. condensated gas state material recovery system as claimed in claim 9, it is characterized in that steam on described jet mixing room or other gaseous material suction inlets are one or more, when the quantity of described steam or other gaseous material suction inlets is one, described steam or other gaseous material suction inlets are provided with the appendix interface forming described steam or other gaseous material imports, when described steam or other gaseous material suction inlets are multiple, described multiple steam or other gaseous material suction inlets are symmetrically distributed on a face of cylinder on the sidewall of described jet mixing room, spacing between adjacent steam or other gaseous material suction inlets is all equal or all not identical, each described steam or other gaseous material suction inlets are connected to respective gas transmission arm, the axis of each described gas transmission arm lays respectively at same surface of revolution on the bus at position, respective place, the top of each described gas transmission arm converges at a common appendix connecting portion, described appendix connecting portion is directly over described power drive room or the rear end of direction of flow be provided with the appendix interface forming described steam or other gaseous material imports.
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| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201510167919.4A CN104874198B (en) | 2015-04-10 | 2015-04-10 | It is suitable to the condensated gas state material recovery method and recovery system of tail gas and flue gas |
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| CN201510167919.4A CN104874198B (en) | 2015-04-10 | 2015-04-10 | It is suitable to the condensated gas state material recovery method and recovery system of tail gas and flue gas |
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| CN104874198B CN104874198B (en) | 2017-03-29 |
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Citations (7)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| GB704580A (en) * | 1951-05-22 | 1954-02-24 | Standard Oil Dev Co | Improvements in or relating to condensing gases by direct contact with immiscible cooling liquids |
| DE4223392A1 (en) * | 1992-07-16 | 1994-01-20 | Dietrich Fette | Condenser for steam component in vapour and air mixts. - has direct flow condenser in front of counter flow condenser to give containers with small cross-section and reduced coolant water consumption |
| JP2011161420A (en) * | 2010-02-15 | 2011-08-25 | Tlv Co Ltd | Exhaust steam recovery apparatus |
| WO2011114084A1 (en) * | 2010-03-16 | 2011-09-22 | Psi Innovation Limited | A vapour recovery apparatus and a method of recovering vapour comprising a vortex tube |
| CN202933507U (en) * | 2012-12-06 | 2013-05-15 | 石家庄海力精化有限责任公司 | Device for recycling gas by using wet method |
| CN204017626U (en) * | 2014-09-01 | 2014-12-17 | 天津市祥泰带钢有限公司 | A kind of hydrometallurgic recovery gas device |
| CN204637632U (en) * | 2015-04-10 | 2015-09-16 | 顾卫荣 | Be suitable for the condensated gas state material recovery system of tail gas and flue gas |
-
2015
- 2015-04-10 CN CN201510167919.4A patent/CN104874198B/en active Active
Patent Citations (7)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| GB704580A (en) * | 1951-05-22 | 1954-02-24 | Standard Oil Dev Co | Improvements in or relating to condensing gases by direct contact with immiscible cooling liquids |
| DE4223392A1 (en) * | 1992-07-16 | 1994-01-20 | Dietrich Fette | Condenser for steam component in vapour and air mixts. - has direct flow condenser in front of counter flow condenser to give containers with small cross-section and reduced coolant water consumption |
| JP2011161420A (en) * | 2010-02-15 | 2011-08-25 | Tlv Co Ltd | Exhaust steam recovery apparatus |
| WO2011114084A1 (en) * | 2010-03-16 | 2011-09-22 | Psi Innovation Limited | A vapour recovery apparatus and a method of recovering vapour comprising a vortex tube |
| CN202933507U (en) * | 2012-12-06 | 2013-05-15 | 石家庄海力精化有限责任公司 | Device for recycling gas by using wet method |
| CN204017626U (en) * | 2014-09-01 | 2014-12-17 | 天津市祥泰带钢有限公司 | A kind of hydrometallurgic recovery gas device |
| CN204637632U (en) * | 2015-04-10 | 2015-09-16 | 顾卫荣 | Be suitable for the condensated gas state material recovery system of tail gas and flue gas |
Also Published As
| Publication number | Publication date |
|---|---|
| CN104874198B (en) | 2017-03-29 |
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Effective date of registration: 20220817 Address after: South side of West Section of Gongye 6th Road, Economic Development Zone, Yangxin County, Binzhou City, Shandong Province, 251800 Patentee after: Shandong Yangxin Xingye Oil Chemical Co., Ltd. Address before: 251800 no.377, Gongye 2nd Road, economic development zone, Yangxin County, Binzhou City, Shandong Province Patentee before: Shandong xinkaiyuan Technology Innovation Development Co.,Ltd. |