CN101432847B - Byproduct collecting apparatus of semiconductor apparatus - Google Patents
Byproduct collecting apparatus of semiconductor apparatus Download PDFInfo
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- CN101432847B CN101432847B CN2007800148666A CN200780014866A CN101432847B CN 101432847 B CN101432847 B CN 101432847B CN 2007800148666 A CN2007800148666 A CN 2007800148666A CN 200780014866 A CN200780014866 A CN 200780014866A CN 101432847 B CN101432847 B CN 101432847B
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- H—ELECTRICITY
- H10—SEMICONDUCTOR DEVICES; ELECTRIC SOLID-STATE DEVICES NOT OTHERWISE PROVIDED FOR
- H10P—GENERIC PROCESSES OR APPARATUS FOR THE MANUFACTURE OR TREATMENT OF DEVICES COVERED BY CLASS H10
- H10P95/00—Generic processes or apparatus for manufacture or treatments not covered by the other groups of this subclass
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D45/00—Separating dispersed particles from gases or vapours by gravity, inertia, or centrifugal forces
- B01D45/04—Separating dispersed particles from gases or vapours by gravity, inertia, or centrifugal forces by utilising inertia
- B01D45/08—Separating dispersed particles from gases or vapours by gravity, inertia, or centrifugal forces by utilising inertia by impingement against baffle separators
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D51/00—Auxiliary pretreatment of gases or vapours to be cleaned
- B01D51/02—Amassing the particles, e.g. by flocculation
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D8/00—Cold traps; Cold baffles
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- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F16—ENGINEERING ELEMENTS AND UNITS; GENERAL MEASURES FOR PRODUCING AND MAINTAINING EFFECTIVE FUNCTIONING OF MACHINES OR INSTALLATIONS; THERMAL INSULATION IN GENERAL
- F16L—PIPES; JOINTS OR FITTINGS FOR PIPES; SUPPORTS FOR PIPES, CABLES OR PROTECTIVE TUBING; MEANS FOR THERMAL INSULATION IN GENERAL
- F16L55/00—Devices or appurtenances for use in, or in connection with, pipes or pipe systems
- F16L55/07—Arrangement or mounting of devices, e.g. valves, for venting or aerating or draining
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D2258/00—Sources of waste gases
- B01D2258/02—Other waste gases
- B01D2258/0216—Other waste gases from CVD treatment or semi-conductor manufacturing
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- Chemical Kinetics & Catalysis (AREA)
- Engineering & Computer Science (AREA)
- General Engineering & Computer Science (AREA)
- Mechanical Engineering (AREA)
- Treating Waste Gases (AREA)
- Chemical Vapour Deposition (AREA)
- Vaporization, Distillation, Condensation, Sublimation, And Cold Traps (AREA)
Abstract
Provided is a byproduct collecting apparatus of semiconductor device for efficiently collecting reaction-byproducts contained in an exhaust gas exhausted from a process chamber during a semiconductor manufacturing process. The apparatus includes a housing and a trap module. The housing has a gas inlet port and a gas outlet port. The trap module is installed inside the housing and has first plates curved or inclined to guide an exhaust gas flow in a curved fashion.
Description
Technical field
The present invention relates to the byproduct gathering-device, it is used for being collected in effectively the reaction by-product that semiconductor fabrication is comprised from the waste gas that process chamber is discharged.
Background technology
Usually, semiconductor fabrication is divided into preprocessing process (manufacture process) and last handling process (assembling process).Preprocessing process is meant through forming predetermined pattern makes the process of semiconductor chip, and this predetermined pattern forms through repeating following process: in various process chambers on wafer deposit film, and the film that optionally etching deposited.Last handling process is meant through produced chip in the preprocessing process is separated into independently chip, and with these independently chip combine with lead frame (lead frame), thereby the process of assembling out complete product.About this respect, carry out etched process in process chamber and at high temperature use such as toxic gases such as silane, arsenic hydride (arsine) and boron chlorides and such as processing gases such as hydrogen and carry out at deposit film on the wafer or to being deposited on film on the wafer.In preprocessing process, in process chamber, understand the toxic gas that produces a large amount of various inflammable gases, corrosive impurities and comprise toxic component.
Therefore, semiconductor manufacturing facility comprises gas cleaner, and this gas cleaner is positioned at the rear end that is used for producing at process chamber the vacuum pump of vacuum state.The waste gas that this gas cleaner will also will purify from the waste gas purification that process chamber is discharged is discharged to the atmosphere.Yet when the waste gas of discharging from process chamber contacted with atmosphere that perhaps ambient temperature is very low, waste gas just can solidify and be transformed into powder.Thereby this powder adherence has increased blowdown presssure on discharge pipe line, simultaneously, when powder gets into vacuum pump, can cause the vacuum pump imbalance, thereby and causes the backflow of waste gas to pollute the wafer that is placed in the process chamber.
Be head it off, shown in figure 14, the waste gas that is used for discharging from process chamber 1 is installed between process chamber 1 and vacuum pump 2 is transformed into pulverous powder trap unit.That is to say that shown in figure 14, process chamber 1 is connected with vacuum pump 3 through aspiration line 5.Catch pipeline 7 and come out, and be used to catch and gather reaction by-product from the powder type of process chamber 1 generation from aspiration line 5 branches.
In traditional powder trap unit; Deposition or the unreacting gas that produced during etch thin film flow to aspiration line 5 in process chamber 1; This aspiration line 5 is compared with process chamber 1 has relatively low ambient temperature; Therefore above-mentioned unreacting gas is solidified into powder 9, and accumulates in from what aspiration line 5 branches came out and catch the pipeline 7.
Yet above-mentioned traditional powder trap unit has following problem.
At first, need for a long time, so cycle period (TAT) is also corresponding has prolonged because the reaction by-product that in process chamber, produces is transformed into powder and accumulates to catch in the pipeline.That is to say, up to be transformed into powder apace at deposition or the reaction by-product that produced during etch thin film and accumulate to catch in the pipeline after, just can carry out next thin film deposition or etching process, need for a long time but reaction by-product is transformed into powder.Therefore, be removed after-processing chamber up to all reaction by-products and just can carry out next process, and want standby for a long time.Therefore, not only the operating rate of equipment reduces, and owing to the long TAT that causes of stand-by time of process chamber prolongs.
Secondly, because it is very narrow to be used to gather the collecting zone of catching pipeline (space) of powder, thereby must remove continually to accumulate in and catch ducted powder, this is very inconvenient.Especially, because powder only concentrated and accumulate in the porch of catching pipeline, thereby it is very short to catch the cleaning cycle of pipeline.
Summary of the invention
The technical problem that solves
The present invention provides a kind of byproduct gathering-device that can collect reaction by-product fast.
The present invention also provides a kind of byproduct gathering-device with longer replacement cycle.
Technical scheme
Embodiments of the invention provide the byproduct gathering-device, and it comprises: the housing with air inlet and gas outlet; And trapping module, it is installed in the said housing, thereby and have and be first plate that bending or skewed direct exhaust flow with bending or inclination mode; Wherein, First plate of said trapping module is radial setting, and said trapping module also comprises a plurality of second plates, and said second plate is installed in the said housing and is formed direct exhaust and flows with zigzag; Said trapping module also comprises: first catches portion, and said first plate is installed in said first and catches in the portion; And second catch portion, and said second plate is installed in said second and catches in the portion, and said second plate is separated and had a plurality of openings by multistage setting and by predetermined space, and said a plurality of openings are set to the passage that lets exhaust flow cross.
In other embodiments, said second portion that catches compares with said first portion of catching and is set at the position that is adjacent to said gas outlet.
In other embodiments; Said first plate has the outer surface that contacts with the inner surface of said housing; And on the outer surface of said first plate, be formed with cutting part, thereby let waste gas between the outer surface of the inner surface of said housing and said first plate, flow.
In other embodiments, on said first plate, be formed with a plurality of through holes, and the size of said through hole becomes big along with the distance of said through hole and said air inlet and reduces.
In other embodiments, said trapping module also comprises: inner core, and it has the inner passage that lets exhaust flow cross, and said first plate and said second plate are fixed on the periphery of said inner core; And the 3rd catch portion, and it is installed in the inner passage of said inner core, thereby collect the reaction by-product of the waste gas that from said inner passage, flows through.
In other embodiments, said the 3rd portion of catching comprises: the support bar of center that vertically is arranged on the inner passage of said inner core; Be mounted obliquely within the 3rd plate on the said support bar; And flatly be installed in the 4th plate on the said support bar.
In other embodiments, said byproduct gathering-device also comprises block piece, and said block piece is used to prevent that passing through said gas outlet from the bulk powder that said trapping module drops discharges.
In certain embodiments, said block piece comprises: stop border (blocking threshold) and the barrier plate that places top, said gas outlet from housing one side that is provided with said gas outlet what protrude facing to the inboard direction of said housing.
In other embodiments, said housing also comprises: cylindrical body, and open its upper and lower; Upper plate, the upper junction of itself and said main body merge and have said air inlet; And lower plate, the lower junction of itself and said main body merges and has said gas outlet.
In other embodiments, said byproduct gathering-device also comprises cooling-part, and said cooling-part has first cooling end that is used to cool off said housing; And second cooling end that is used to cool off the inner core of said trapping module.
In other embodiments, said first cooling end comprises the cooling of first on the wall that is arranged on said housing pipeline, and said second cooling end comprises the second cooling pipeline on the wall that is arranged on said interior letter.
In other embodiments, said byproduct gathering-device also comprises the heater block that is used for heating the waste gas that is introduced in said housing.
In other embodiments of the invention, the byproduct gathering-device comprises: housing, the inner passage that it has air inlet, gas outlet and lets exhaust flow cross; Cooling tower, it is installed in the said housing; And trapping module, it is arranged in the said housing, thereby and have the lip-deep reaction by-product that a plurality of plates are collected said a plurality of plates, also comprise the cooling-part that is used to cool off said housing and said cooling tower.
In other embodiments of the invention, the byproduct gathering-device comprises: the housing with air inlet and gas outlet; Be located at first in the said housing and catch portion, and catch said first and to be provided with first plate that is used to collect reaction by-product in the portion; Be located at second in the said housing and catch portion; And catch said second and to be provided with second plate that is used to collect reaction by-product in the portion; Wherein said first plate and said second plate are shaped as direct exhaust and flow in different directions; Wherein, flow with bend mode thereby each said first plate has the tilted shape direct exhaust, each said second plate is configured to vertical with the longitudinal direction of said housing; Said second plate is separated by predetermined space and is faced with each other, thereby and in said second plate, is formed with opening gas is flowed with zigzag.
In other embodiments, being shaped as of said first plate: when flowing on the longitudinal direction of waste gas at said housing, this shape lets waste gas not carry out perpendicular flow.
In other embodiments, being shaped as of said first plate: when flowing on the longitudinal direction of waste gas at said housing, this shape lets waste gas flow with bend mode.
In other embodiments, each said first plate is installed to be and has 50 °～60 ° gradient with respect to the longitudinal direction of said housing.
Beneficial effect
The present invention utilizes the dual-cooled line construction thereby has the special result of cooling reaction byproduct more quickly.
The present invention can through in the outer surface of housing and inner surface simultaneously the cooling reaction byproduct improve the collection efficiency of reaction by-product.
The present invention has following advantage: be divided into annular space and central space through the inner space with housing, and in each space, the plate with different shape be set, thereby utilize the powder binding domain of widening to make the collecting amount maximization.
According to the present invention, because powder is collected on the whole trapping module equably, therefore can prolong the work period of gathering-device, and can solve the productivity ratio reduction problem that causes owing to the caused work interruption of frequent change.
Thereby the present invention can be through preventing to discharge the damage that prevents vacuum pump through the gas outlet from the powder block that collection module drops.
Description of drawings
Fig. 1 is the view of outward appearance that the byproduct gathering-device of the embodiment of the invention has been described;
Fig. 2 is the partial sectional view of byproduct gathering-device;
Fig. 3 is the exploded perspective view of byproduct gathering-device;
Fig. 4 is the end view that the byproduct gathering-device has been described;
Fig. 5 is the sectional view along the A-A line among Fig. 4;
Fig. 6 is the exploded perspective view of trapping module;
Fig. 7 is the end view of trapping module;
Fig. 8 is the stereogram that portion is caught in the 3rd of modification;
Fig. 9 has the stereogram that the trapping module of portion is caught in the 3rd of modification;
Figure 10 is the partial sectional view that the byproduct gathering-device of trapping module shown in Figure 9 is installed;
Figure 11 has explained among Figure 10 that the 3rd catches the view of the 6th plate of portion;
Figure 12 has explained by the photo of the reaction by-product of trapping module collection of the present invention;
Figure 13 is the photo that the reaction by-product of the trapping module collection that is equipped with multistage plate has been described; And
Figure 14 is the skeleton diagram that the byproduct gathering-device of prior art has been described.
Embodiment
The structure of gathering-device of the present invention can let waste gas also pass through the complicated and narrow passage at the place, rear portion through the simple and wide passage of forwardly locating, thereby powder not only can be accumulated in equably on the front portion, also can accumulate on the rear portion equably.In addition, the structure of gathering-device of the present invention can also be carried out dual-cooled with inboard to the temperature of waste gas in the outside of housing, thereby reduces the temperature of waste gas more quickly.
Fig. 1 is the view of outward appearance that the byproduct gathering-device of the embodiment of the invention has been described; Fig. 2 is the partial sectional view of byproduct gathering-device; Fig. 3 is the exploded perspective view of byproduct gathering-device; Fig. 4 is the end view that the byproduct gathering-device has been described, and Fig. 5 is the sectional view along the A-A line among Fig. 4.
This byproduct gathering-device is installed in the rear end of the pump on the discharge pipe line of process chamber, when deposition or etch thin film in semiconductor or liquid crystal display manufacture process or similar procedure, in said process chamber, can produce reaction by-product.
With reference to Fig. 1～Fig. 5, byproduct gathering-device 100 comprises housing 110, heater block 120, trapping module 130 and cooling-part 170.
As stated, be easy to separate and assembled construction, therefore be convenient to the maintenance of housing 110 because housing 110 has.For example, thus be deposited on the inwall (inwall of main body 112) of housing 110 and the powder on the trapping module through housing 110 being safeguarded remove.
With reference to Fig. 2, Fig. 5～Fig. 7, trapping module 130 is unusual important components in powder collection.Trapping module 130 comprises that first catches portion 134, second and catch portion the 142, the 3rd and catch portion 150 and inner core 132.
That is to say that the inner space of housing 110 is divided into corresponding to the annular space a1 in inner core 132 outsides with corresponding to the interior central space a2 of inner core 132 inboards (inner passage) by inner core 132.A part is introduced in exhaust flow in the inner space of housing 110 to annular space a1, and remaining exhaust flow is to interior central space a2.First catches portion 134 and second catches portion 142 and is positioned at annular space a1.The 3rd catches portion 150 is positioned at interior central space a2.The temperature that flows to the waste gas of annular space a1 receives the temperature effect of housing 110 and inner core 132 and descends.The temperature that flows to the waste gas of interior central space a2 (inner passage of inner core) receives the temperature effect of inner core 132 and descends.As stated, in the present invention, because the waste gas of process is cooled off equably from the inner space of housing 110, so trapping module 130 can more effectively change reaction by-product powder into and collect powder.
As stated, powder collection device 130 of the present invention is characterised in that, it not only has and comprises housing 110 and be positioned at the structure of the inner core 132 of housing 110, but also has the multiple cooling structure that housing 110 and inner core 132 all are cooled.
First catches portion 134 comprises and is radial (with 60 ° interval) and is mounted obliquely within six first plates 136 on the periphery of inner core 132.Thereby first plate 136 is the curved shape direct exhaust to flow with bend mode.First plate 136 is opened so that waste gas can flow apace with enough separating distances.That is to say, sweeping first plate is mounted obliquely within on the periphery of inner core.About this respect, first plate 136 can be installed by 50 °～60 ° pre-determined tilt angle.For example, when the gradient of first plate 136 very when big (that is, first plate 136 is almost set level), powder only concentrates on first plate 136.On the other hand, when the gradient very little (that is, first plate, 136 nearly erects) of first plate 136, powder can not accumulate on first plate 136, but only accumulates on second plate.Simultaneously, first plate 136 comprises a plurality of through hole 136a.The size of through hole 136a can become big and reduce along with the distance of these through holes 136a and air inlet 114a.Because inwall 112a (that is, the inwall of the main body) contact of the outer surface of first plate 136 137 and housing 110, thereby be easy to carry out the heat exchange with housing 110.That is to say that first plate 136 is cooled through inner core 132 and housing 110.First plate 136 comprises cutting part 136b, and this cutting part 136b forms through a part of cutting away first plate 136 along outer surface 137.For example, first plate 136 can have writing board shape and on the periphery of inner core, tilt at a predetermined angle.
Below explanation first catch portion 134 places exhaust-gas flow.Waste gas flows when turning to along the bending channel between first plate 136.Part waste gas is downward through the through hole 136a and the cutting part 136b of first plate 136.For waste gas is flowed fast, first catches portion 134 also provides a plurality of additional vertical passages except main ramp way is provided.
Shown in accompanying drawing, first catch portion 134 length greater than second catch portion 142 length.For example, first catch the length ratio that portion 134 and second catches portion 142 and can be 7:3.For example, when catching length ratio that portion and second catches portion when being controlled to be 5:5 with first, reaction by-product can occur and concentrate on first phenomenon of catching in the portion.This phenomenon possibly be to produce owing to byproduct accumulates in first portion of catching place.This byproduct gather can by first catch first plate of portion angle of inclination and the second long moving conduit of catching portion cause.
The 3rd catches among the inner passage a2 that portion 150 is installed in inner core 132.The 3rd catches portion 150 designed to be used the waste gas that collection flows through from the inner passage a2 of inner core 132 reaction by-product.The 3rd catches portion 150 comprises: 152, four of support bars that vertically are arranged at the a2 center, inner passage of inner core 132 are mounted obliquely within the 3rd plate 154 on the support bar 152, and flatly are installed in the 4th plate 156 on the support bar 152.Use three bolts that the top of support bar 152 is combined with inner core 132.Each the 4th plate 154 is installed on the support bar by six rank.Therefore that the 4th plate 154 that is installed in bottom is formed circle, do not have bulk powder to drop to gas outlet 116a, and the outer surface of that the 4th plate is formed curved shape so that combustion gas easily.
Fig. 8～Figure 11 has explained that the 3rd catches the view of the various modifications of portion.
Fig. 8 has explained and has comprised support bar 152 and catch the 150a of portion by multistage the 3rd of the 4th plate 158 on the support bar 152 that is installed in.In addition, Fig. 9～Figure 11 has explained and has comprised that the 3rd of six the 5th plates 159 with through hole 159a and level the 6th plate 160 catch the 150a of portion.The 5th plate 159 is tilted placement with respect to the inner passage a2 of inner core 132, and is installed to be the inboard that makes these the 5th plates and contacts with the inner surface 132a of inner core 132.In addition, the 6th plate 160 is installed to be multistage, and is being supported by the upper surface of three support bars 161 from lower plate 116.
Simultaneously, byproduct gathering-device of the present invention comprises block piece.Said block piece blocks powder, the bulk powder that therefore breaks away from from trapping module 130 can not released through gas outlet 116a.Said block piece comprise from the inner surface of lower plate 116 protruding upward stop border 162.The said border that stops is designed to stop the bulk powder of direction introducing from the side.For example, this block piece can be installed in the 3rd and catch portion 130 places.Shown in Figure 6 be positioned at the 3rd and catch the 4th plate 154 that portion 150 locates bottom and be positioned at the 3rd and catch the 6th plate that the 150b of portion locates bottom as barrier plate with shown in Figure 10.
Although, when too much plate is installed, can hinder flowing fast of waste gas for not restriction of the quantity that is installed in the plate in the trapping module 130.In addition, under the too narrow situation in the interval between each plate, can very fast blocking channel when powder deposition.Therefore, to considering comprehensively, come suitably to select the quantity of the plate installed through on the whole such as installation environment, enclosure interior pressure and the various factorss such as processing that will carry out.
As stated; Byproduct gathering-device of the present invention is characterised in that; Through letting simple and wide moving conduit and the complicated and narrow moving conduit through at rear portion locate of waste gas, can make powder not only be deposited on anterior place equably, and be deposited on the place, rear portion equably through forwardly locating.In other words, through the low temperature environment of housing 110, the reaction by-product that is incorporated into the waste gas in the housing 110 is transformed into powder.About this respect, when waste gas is caught inclination and the wide moving conduit of portion 134 through first, change and a part of powder of coming accumulates in first and catches on the outer surface and inner core 132 of first plate 136 of portion 134 from this waste gas.In addition, when waste gas through by second catch portion 142 second plate 144 provide complicated and narrow moving conduit the time, through first catch the waste gas of portion 134 all the other powder accumulate on the periphery of surface and inner core 132 of second plate 144.
Cooling-part 170 is designed to make housing 110 inside to become low temperature environment, so that catch the reaction by-product that is included in the waste gas that is incorporated in the housing 110.With reference to accompanying drawing; Cooling-part 170 comprises: the first cooling pipeline 172 that is used to cool off the main body 112 of housing 110; Be used to cool off the second cooling pipeline 174 of the inner core 132 of trapping module 130; Be used for supply line 176, and be used to discharge the discharge line 177 that cools off the cooling agent of pipeline through each to the first cooling pipeline 172 and the second cooling pipeline, 174 supply coolants.
Here, the surface that the first cooling pipeline 172 and the second cooling pipeline 174 not only cool off housing 110 and inner core 132, but also the temperature of each plate of the internal temperature of reduction housing 110 and trapping module 130.In the time of in cooling agent being incorporated into the first cooling pipeline 172 and the second cooling pipeline 174, the internal temperature of housing 110, inner core 132 and each plate 136,144,154 are compared with the temperature of waste gas all and can be reduced significantly and relatively with 156 temperature.
Therefore, waste gas (particularly reaction by-product) is introduced in the housing 110 and by heater block 120 and heats.When the waste gas that is in gaseous state at once with the housing that is cooled to low temperature 110, inner core 132 and each plate 136,144,154 when 156 surface contacts, this waste gas is transformed into one deck immediately and is deposited, and therefore can carry out gas sampling rapidly.Here; The reaction by-product that when waste gas is deposited on trapping module 130 surfaces, is produced is transformed into that time when solid-state from gaseous state; This reaction by-product be transformed into one deck and more rapidly, evenly and firmly deposit to each plate 136,144,154 and 156 and the surface of inner core 132 on.
Especially, through the first cooling pipeline 172 and the second cooling pipeline 174 housing 110 and inner core 132 are cooled off, thereby promptly reduce the internal temperature of housing 110 and the surface temperature of each plate 136,144,154 and 156.First plate 136 is installed to be with the inwall of housing 110 and the outer wall of inner core 132 with second plate 144 and contacts, and the 3rd plate 154 is installed to be with the inwall of inner core 132 with the 4th plate 156 and contacts, thereby increases the heat exchange area of each plate 136,144,154 and 156.Thereby, formed and can solidify the environment that is introduced in the reaction by-product in the housing 110 more quickly.
As stated, the structure of byproduct gathering-device of the present invention can be introduced in the reaction by-product in the said housing thereby more promptly solidify at the outside and the inner dual-cooled reaction by-product of housing.
The work of the byproduct gathering-device that in semiconductor equipment, has said structure is described with reference to the accompanying drawings.
At first, through the cooling agent supply line 40 that links to each other with the external refrigeration agent container cooling agent is supplied to the first cooling pipeline 410 and the second cooling pipeline 420.When cooling agent flow through the first and second cooling pipelines, the surface temperature of housing, inner core and each plate and the internal temperature of housing all descended.In addition, because the heater 220 of heater block is worked and given out heat of high temperature, the heating plate 210 that therefore contacts with heater 220 is heated to high temperature.When the byproduct gathering-device was worked, the waste gas that contains a large amount of reaction by-products that produce from the process chamber that is connected with said gathering-device was introduced in the housing via air inlet.This waste gas is heated the parts heating and is diffused in the inner space of housing 110.
A part has been diffused into exhaust flow in the inner space of housing 110 to annular space a1, and remaining exhaust flow is to central space a2.Flowing to this part waste gas of annular space a1 contacts with the inwall of the housing that is cooled to low temperature 110, the outer wall surface of first plate and the outer wall surface of inner core.When that time that the outer wall surface of the outer wall surface of the inwall of this part waste gas and housing 110, first plate and inner core contacts, this part waste gas just is cooled, and the process that promptly takes place to solidify from gaseous state, is being deposited on each surface.
In addition, that part of waste gas that flows to central space (the inner passage a2 of inner core) contacts with the inwall of the inner core that is cooled to low temperature and the surface of the 3rd plate.When that time that the surface of the inwall of that part of waste gas that flows to central space and inner core and the 3rd plate contacts, that part of waste gas just is cooled, and the process that promptly takes place to solidify from gaseous state, is being deposited on each surface.
Operate because structure of the present invention can be as stated be carried out dual-cooled in the outside of housing with inside, so the internal temperature of housing can be maintained low temperature, thereby reaction by-product can more promptly solidify.As a reference, when temperature reduced rapidly, the reaction by-product of gaseous state was transformed into the powder with strong characterization of adsorption.Especially, reaction by-product has stronger characterization of adsorption at the part place that is cooled to below the predetermined temperature.Therefore, the reaction by-product of the inner space of process housing 110 is by cooling promptly, thereby trapping module 130 can more effectively be transformed into reaction by-product powder and collect powder.
Simultaneously; When other reaction by-products of collecting when first portion of catching that obtains module at large are caught horizontal channel and the vertical channel of portion with zigzag through second; These reaction by-products are cooled to below the predetermined temperature, take place to solidify and accumulate on the inwall of outer wall and housing of surface, inner core of second plate.In addition, when be not collected into the 3rd catch portion's upper end other reaction by-products when catching the 4th plate of portion through the 3rd with zigzag, these reaction by-products take place to solidify and accumulate on the inwall of surface and inner core of the 4th plate.Therefore, shown in figure 12, powder is deposited on the whole trapping module equably.With reference to Figure 13, because powder only accumulates on the upper surface of upper plate at the top place that is positioned at the trapping module that multistage discoid plate is installed, therefore not only the replacement cycle is very short, and collection efficiency obviously reduces.
That is to say; The structure of byproduct gathering-device of the present invention can let waste gas also pass through the complicated and narrow moving conduit at the place, rear portion through the simple and wide moving conduit of forwardly locating; Thereby powder not only can be accumulated on the front portion equably, and can accumulate on the rear portion equably.Therefore, obviously prolonged the replacement cycle of gathering-device, thereby reduced processing delay, improved productivity ratio and reduced manufacturing cost.
Above-mentioned disclosed theme should be considered to illustrative rather than restrictive, and accompanying claims is intended to cover all changes, improvement and other embodiment that falls in true spirit of the present invention and the scope.Therefore, allow to the full extent at law, scope of the present invention is allowed to explain accompanying claims and equivalent thereof the wideest and limits, and do not receive above-mentioned constraint that specifies or restriction.
Application in industry
The present invention can be applicable to the equipment of ownership manufacturing semiconductor and LCD.Especially; Thereby byproduct gathering-device of the present invention is applied in and collects the reaction by-product that is disposed to said discharge pipe line on the discharge pipe line of process chamber effectively; In said process chamber; When deposition or etch thin film in semiconductor, LCD manufacture process or other similar processing procedures, can produce reaction by-product.
Claims (29)
1. device that is used for being collected in the reaction by-product that waste gas comprised that process chamber produces, said device comprises:
Housing, it has air inlet and gas outlet; And
Trapping module, it is installed in the said housing, thereby and have and be first plate that bending or skewed direct exhaust flow with bend mode,
Wherein, first plate of said trapping module is radial and is provided with obliquely,
Said trapping module also comprises a plurality of second plates, and said second plate is installed in the said housing and is shaped as direct exhaust and flows with zigzag,
Said trapping module comprises:
First catches portion, and said first plate is installed in said first and catches in the portion; And
Second catches portion, and said second plate is installed in said second and catches in the portion, and said second plate is separated and had a plurality of openings by multistage setting and by predetermined space, and said a plurality of openings are set to the passage that lets exhaust flow cross.
2. device as claimed in claim 1, wherein said first catch portion length greater than said second catch portion length.
3. device as claimed in claim 1, wherein said second portion that catches compares with said first portion of catching and is set at the position that is adjacent to said gas outlet.
4. device as claimed in claim 1; Wherein said first plate has the outer surface that contacts with the inner surface of said housing; And on the outer surface of said first plate, be formed with cutting part, thereby let waste gas between the outer surface of the inner surface of said housing and said first plate, flow.
5. device as claimed in claim 1 wherein is formed with a plurality of through holes on said first plate.
6. device as claimed in claim 5, the size of wherein said through hole becomes big along with the distance of said through hole and said air inlet and reduces.
7. device as claimed in claim 1, wherein said trapping module also comprises:
Inner core, it has the inner passage that lets exhaust flow cross, and wherein said first plate and said second plate are fixed on the periphery of said inner core, and
The 3rd catches portion, and it is installed in the inner passage of said inner core, thereby collects the reaction by-product of the waste gas that from said inner passage, flows through.
8. device as claimed in claim 7, wherein said the 3rd portion of catching comprises:
Vertically be arranged on the support bar of center of the inner passage of said inner core;
Be mounted obliquely within the 3rd plate on the said support bar; And
Flatly be installed in the 4th plate on the said support bar.
9. device as claimed in claim 7 also comprises block piece, and said block piece is used to prevent that passing through said gas outlet from the bulk powder that said trapping module drops discharges.
10. device as claimed in claim 9, wherein said block piece comprise and stop the border that it is protruding facing to the inboard direction of said housing from housing one side that is provided with said gas outlet.
11. device as claimed in claim 10, wherein said block piece also comprise the barrier plate that places top, said gas outlet.
12. device as claimed in claim 1, wherein said housing comprises:
Cylindrical body, open its upper and lower;
Upper plate, the upper junction of itself and said main body merge and have said air inlet; And
Lower plate, the lower junction of itself and said main body merge and have said gas outlet.
13. device as claimed in claim 7 also comprises the cooling-part that is used for cooling off the waste gas that flows through from said housing.
14. device as claimed in claim 13, wherein said cooling-part comprises:
Be used to cool off first cooling end of said housing; And
Be used to cool off second cooling end of the inner core of said trapping module, wherein said first plate and said second plate with by the said housing and the said inner core heat-shift of said cooling-part cooling.
15. device as claimed in claim 14, wherein said first cooling end comprise the cooling of first on the wall that is arranged on said housing pipeline, and said second cooling end comprises the cooling of second on the wall that is arranged on said inner core pipeline.
16. device as claimed in claim 1 also comprises the heater block that is used for heating the waste gas that is introduced in said housing.
17. a device that is used for being collected in the reaction by-product that waste gas comprised that process chamber produces, said device comprises:
Housing with air inlet and gas outlet;
Be located at first in the said housing and catch portion, wherein catch on the surface of portion first plate that is used to collect reaction by-product is installed said first;
Be located at second in the said housing and catch portion, wherein catch on the surface of portion second plate that is used to collect reaction by-product is installed, and said first plate and said second plate be shaped as direct exhaust and flow in different directions said second,
Wherein thereby each said first plate has the tilted shape direct exhaust and flows with bend mode; Each said second plate is configured to vertical with the longitudinal direction of said housing; Said second plate is separated by predetermined space and is faced with each other, thereby and in said second plate, is formed with opening gas is flowed with zigzag.
18. device as claimed in claim 17, wherein each said first plate is installed to be and has 50 °～60 ° gradient with respect to the longitudinal direction of said housing.
19. device as claimed in claim 17, being shaped as of wherein said first plate: when flowing on the longitudinal direction of waste gas at said housing, this shape lets waste gas not carry out perpendicular flow.
20. device as claimed in claim 17, being shaped as of wherein said first plate: when flowing on the longitudinal direction of waste gas at said housing, this shape lets waste gas flow with bend mode.
21. a device that is used for being collected in the reaction by-product that waste gas comprised that process chamber produces, said device comprises:
Housing, the inner passage that it has air inlet, gas outlet and lets exhaust flow cross;
Cooling tower, it is installed in the said housing; And
Trapping module, it is arranged in the said housing, thereby and have a lip-deep reaction by-product that a plurality of plates are collected said a plurality of plates,
Also comprise the cooling-part that is used to cool off said housing and said cooling tower.
22. device as claimed in claim 21, wherein said cooling tower is formed tubular, thereby said inner passage is divided into annular space and interior central space.
23. like claim 21 or 22 described devices, wherein said a plurality of plates abut against on the outer surface of inner surface and said cooling tower of said housing.
24. like claim 21 or 22 described devices, wherein said a plurality of plates comprise and are shaped as first plate and second plate that direct exhaust flows in different directions.
25. device as claimed in claim 24, wherein said trapping module comprises:
First catches portion, and said first plate is installed in said first and catches in the portion; And
Second catches portion, and said second plate is installed said second and caught in the portion, thereby wherein said first plate is bending or plane direct exhaust flows with bend mode, and said second plate has the shape that direct exhaust flows with zigzag.
26. device as claimed in claim 25, wherein said first plate are radial and are provided with obliquely.
27. device as claimed in claim 22 also comprises the 3rd plate, it is installed in the central space of said cooling tower, thereby collects the reaction by-product of the waste gas that from said central space, flows through.
28. like claim 21 or 22 described devices, also comprise block piece, said block piece is used to prevent that passing through said gas outlet from the bulk powder that said trapping module drops discharges.
29. like claim 21 or 22 described devices, wherein said cooling-part comprises:
First cooling end, it has the cooling of first on the wall that is arranged on said housing pipeline; And
Second cooling end, it has the cooling of second on the wall that is arranged on said cooling tower pipeline, wherein said a plurality of plates and the said housing and the said cooling tower heat-shift that are cooled off by said cooling-part.
Applications Claiming Priority (7)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| KR1020060040700A KR100676927B1 (en) | 2006-05-04 | 2006-05-04 | By-product Collector of Semiconductor Device |
| KR1020060040700 | 2006-05-04 | ||
| KR10-2006-0040700 | 2006-05-04 | ||
| KR1020060041531A KR100647725B1 (en) | 2006-05-09 | 2006-05-09 | By-product Collector of Semiconductor Device |
| KR1020060041531 | 2006-05-09 | ||
| KR10-2006-0041531 | 2006-05-09 | ||
| PCT/KR2007/002008 WO2007129820A1 (en) | 2006-05-04 | 2007-04-25 | Byproduct collecting apparatus of semiconductor apparatus |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| CN101432847A CN101432847A (en) | 2009-05-13 |
| CN101432847B true CN101432847B (en) | 2012-05-09 |
Family
ID=38105022
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN2007800148666A Active CN101432847B (en) | 2006-05-04 | 2007-04-25 | Byproduct collecting apparatus of semiconductor apparatus |
Country Status (2)
| Country | Link |
|---|---|
| KR (1) | KR100676927B1 (en) |
| CN (1) | CN101432847B (en) |
Cited By (1)
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| TWI681809B (en) | 2017-12-27 | 2020-01-11 | 南韓商未來寶股份有限公司 | Semiconductor process by-product trapping device |
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| KR100768887B1 (en) | 2007-07-24 | 2007-10-22 | 주식회사 엠아이 | Semiconductor Reaction Byproduct Trap Device |
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| KR100840518B1 (en) | 2007-11-16 | 2008-06-23 | 주식회사 엠아이 | Semiconductor Reaction Byproduct Trap Device |
| KR101024504B1 (en) * | 2009-04-01 | 2011-03-31 | 주식회사 미래보 | Residual Chemical and By-product Collector in Semiconductor Process Using Particle Inertia |
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| CN113663426B (en) * | 2021-08-25 | 2022-07-26 | 湖北玖恩智能科技有限公司 | Powder collecting and filtering device and gas purifying equipment |
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| Publication number | Priority date | Publication date | Assignee | Title |
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| TWI681809B (en) | 2017-12-27 | 2020-01-11 | 南韓商未來寶股份有限公司 | Semiconductor process by-product trapping device |
Also Published As
| Publication number | Publication date |
|---|---|
| CN101432847A (en) | 2009-05-13 |
| KR100676927B1 (en) | 2007-02-02 |
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