JP6538953B1 - Polishing fluid supply device - Google Patents

Abstract

The present invention provides a technical means capable of efficiently adjusting the concentration of slurry in the polishing step of a semiconductor manufacturing process.
SOLUTION: A mixing flow channel 40 detects the flow rate per unit time of the liquid in the mixing flow channel 40, and signals SF1 _SLR , SF1 _CHM , SF1 _H2O2, SF2 _SLR , SF2 _CHM , which indicate the detected flow rate. There are flow sensors 61 _SLR , 62 _SLR , 63 _SLR , 61 _CHM , 62 _CHM , 63 _CHM , 61 _{H 2 O 2} , 62 _{H 2 O 2} , 63 _H 2 _{O 2} that output SF _{2 H} 2 _{O 2} , and the slurry, chemical, and hydrogen peroxide water are transported There are flow controllers 15 _SLR , 15 _CHM and 15 _{H 2 O 2} in the path which adjust the flow rate of the liquid in the flow path according to the given signal SG. The PLC 70, which is a control means, controls the operation of the flow controllers 15 _SLR , 15 _CHM , and 15 _{H 2 O 2} based on the relationship between the flow rate of the liquid in the mixing channel 40 and the target value.
[Selected figure] Figure 1

Description

  The present invention relates to a polishing liquid supply apparatus that supplies a polishing liquid obtained by diluting a slurry to a CMP (Chemical Mechanical Polishing) polishing apparatus.

  In the semiconductor manufacturing process, there is a process called mechanical polishing that etches the etched wafer 88, which is called polishing. FIG. 8 is a view showing a schematic configuration of a CMP system used in this process. As shown in FIG. 8, the CMP system is configured of a polishing apparatus 8 and a polishing liquid supply apparatus 9. The wafer 88 to be polished is bonded to a bonding plate 82 on the lower surface of the head 81 of the polishing apparatus 8. The wafer 88 is pressed against the polishing pad 84 on the surface plate 83 by the head 81. The tank 91 of the polishing liquid supply device 9 stores a polishing liquid obtained by diluting the slurry with ultrapure water or a chemical. When the polishing liquid in the tank 91 of the polishing liquid supply apparatus 9 is sucked by the pump 92 and the head 81 and the platen 83 are rotated while dropping the polishing liquid from the tip of the nozzle 85 onto the polishing pad 84, the wafer 88 becomes the polishing pad 84. The surface of the wafer 88 is polished by the mechanical action of sliding on the polishing pad 84 while being pressed against and the chemical reaction action of the wafer 88 contacting the slurry in the polishing agent. For details of the configuration of the CMP system, refer to Patent Document 1.

  It is known that the polishing shape of the wafer 88 in the CMP system depends on the rotation speed of the polishing pad 84 and the supply performance of the polishing liquid. In order to improve the polishing shape of the wafer 88, it is essential to keep the rotational speed of the polishing pad 84 and the amount of polishing solution supplied per unit time constant. In general, the removal amount increases in proportion to the relative velocity between the wafer 88 and the polishing pad 84 and the processing pressure.

JP, 2017-13196, A

  In the polishing process, in order to increase the consumption efficiency of the slurry, at first, a polishing solution with high slurry concentration is used, and in the finishing stage, a polishing solution with low slurry concentration is used, etc. It is common to selectively use the slurry concentration. However, in a conventional CMP apparatus, a stirring apparatus is installed in a tank of a polishing liquid supply apparatus, a slurry stock solution, ultrapure water, and a chemical agent called chemical are injected into a preparation tank, and these liquids are prepared by the stirring apparatus. Was supplied as a polishing liquid to the polishing apparatus, and the slurry concentration of the liquid once prepared in the tank could not be changed later. For this reason, there is a problem that it takes time to prepare polishing liquids having different slurry concentrations, and it becomes unnecessary to discard the slurry wastefully.

  The present invention has been made in view of such problems, and an object thereof is to provide a technical means capable of efficiently adjusting the concentration of the slurry in the polishing step of the semiconductor manufacturing process.

  In order to solve the above problems, the present invention is a polishing liquid supply apparatus for supplying a polishing liquid to a CMP polishing apparatus, comprising: a first flow path for transferring slurry; and a second flow path for transferring pure water A preparation flow channel disposed immediately before a liquid delivery port leading to the CMP polishing apparatus, which is in communication with the first flow channel and the second flow channel, and includes the slurry and the pure water. A compounding channel for supplying a liquid prepared by mixing a plurality of types of liquids to the CMP polishing apparatus as the polishing liquid, a control means, and a sensor provided in the compounding channel, the liquid in the compounding channel A flow rate sensor for detecting a flow rate or pressure and outputting a signal indicating the detected flow rate or pressure, and a flow controller provided in the first flow path, the first flow path according to a given signal Control to adjust the flow rate or pressure of Comprising the door, said control means, based on the relationship between the flow rate and the target value of the liquid in the regulating merging path, to provide a polishing liquid supply apparatus characterized by controlling the operation of the flow controller.

  According to the present invention, it is possible to efficiently adjust the concentration of the slurry in the polishing step of the semiconductor manufacturing process.

FIG. 1 is a view showing an entire configuration of a CMP system including a polishing liquid supply apparatus according to a first embodiment of the present invention. It is a figure which shows the detail of a structure of the mixing unit of FIG. It is a figure for demonstrating the effect | action in connection with stirring and preparation of the mixing unit of FIG. It is a figure which shows the whole structure of the CMP system containing the polishing liquid supply apparatus which is 2nd Embodiment of this invention. It is a figure which shows the detail of a structure of the mixing unit of the polishing liquid supply apparatus which is a modification of this invention. It is a figure which shows the detail of a structure of the pressurization tank of the polishing liquid supply apparatus which is a modification of this invention. It is a figure which shows the whole structure of the CMP system containing the polishing liquid supply apparatus which is a modification of this invention. It is a figure which shows schematic structure of the conventional CMP system.

  Hereinafter, embodiments of the present invention will be described with reference to the drawings.

First Embodiment
FIG. 1 is a view showing the overall configuration of a CMP system 1 including a polishing liquid supply apparatus 2 according to a first embodiment of the present invention. The solid line connecting the elements in FIG. 1 indicates the pipe, and the arrow on the solid line indicates the traveling direction of the liquid in the pipe. The CMP system 1 is used in the polishing step of the semiconductor manufacturing process. The CMP system 1 includes a CMP polishing apparatus 8 and a polishing liquid supply apparatus 2. The liquid feed port 89 of the CMP polishing apparatus 8 is connected to the liquid delivery port 79 of the polishing liquid supply apparatus 2. The CMP polishing apparatus 8 polishes a wafer 88 to be polished. The polishing liquid supply device 2 supplies the polishing liquid to the CMP polishing device 8.

The polishing liquid is a liquid prepared by mixing a slurry, ultrapure water, a chemical, and a hydrogen peroxide solution at a predetermined ratio. Here, the slurry may be a slurry containing an abrasive or the like, an alkaline slurry containing SiO ₂ , a neutral slurry containing CeO ₂ , or an acidic slurry containing Al ₂ O ₃ . The chemicals include silica, meloic acid, citric acid and the like. The active components of the slurry and the chemical may be determined in accordance with the wafer 88 to be polished and the polishing shape.

The polishing liquid supply device 2 includes a PLC (Programmable Logic Controller) 70, an ultrapure water inlet 29 connected to an external ultrapure water supply source, a drum 12 _CHM in which a chemical is stored, and a drum in which a slurry is stored. 12 _SLR , drum 12 _{H 2 O 2} storing hydrogen peroxide solution, flow path 20 _DIW (second flow path) forming transfer path of ultrapure water, flow path 10 _CHM forming transfer path of chemical, transfer of slurry The flow path 10 _SLR (first flow path) that forms the path, the flow path 10 _{H 2 O 2} that forms the transfer path of the hydrogen peroxide solution, and the four types of liquids: ultrapure water, chemical, slurry, and hydrogen peroxide solution It has a compounding channel 40 to be compounded.

The preparation flow path 40 is disposed immediately before the liquid delivery port 79 leading to the CMP polishing apparatus 8. The preparation channel 40 is in communication with the channel 20 _DIW , the channel 10 _CHM , the channel 10 _SLR , and the channel 10 _{H 2 O 2} . Mixing units 50 _CHM , 50 _SLR , and 50 _{H 2 O 2} , and flow sensors 61 _{CH M} , 62 _CHM , 63 _CHM , 61 _SLR , 62 _SLR , 63 _SLR , 61 _{H 2 O 2} , 62 _{H 2 O 2} , and 63 _{H 2 O 2.} Is provided.

The flow path 20 _DIW is provided with a low pressure valve 21 (precise regulator). By the action of the low pressure valve 21, the flow rate of ultra pure water in the flow path 20 _DIW is kept constant (for example, 1 liter / minute). The end of the pipe forming the flow path 20 _DIW is connected to the inlet F1 of the mixing unit 50 _CHM . The ultrapure water transferred in the flow path 20 _DIW flows into the mixing unit 50 _CHM from the inflow port F1.

In the flow path 10 _CHM , a pump 11 _CHM , a pressure tank 13 _CHM , a filling amount sensor 16 _CHM , a flow controller 15 _CHM , and a gas pressurizing unit 14 _CHM are provided. Pump 11 _CHM is a rotary pump such as a diaphragm pump or a bellows pump. The pump 11 _CHM pumps out the chemical in the drum 12 _CHM and supplies it to the side with the pressurized tank 13 _CHM in the flow path 10 _CHM . Chemicals pumped out by the pump _{11 CHM} is pressurized tank ₁₃ flows into the _CHM, it is filled into the pressure tank ₁₃ in _CHM. The on-off valve VLU is provided at the liquid inlet of the pressurized tank 13 _CHM , and the on-off valve VLL is provided at the liquid outlet. The on-off valves VLU and VLL of the pressurized tank 13 _CHM open when the open signal SV _OP is given, and close when the close signal SV _CL is given.

The filling amount sensor 16 _CHM detects the filling amount of the chemical in the pressure tank 13 _CHM , and outputs a signal indicating the detected filling amount. Specifically, when the filling amount of the chemical in the pressure tank 13 _CHM falls below a predetermined value, the filling amount sensor 16 _CHM outputs a detection signal ST _CHM indicating that.

Gas pressure portion _{14 CHM} under the control of the flow controller _{15 CHM,} the pressure tank ₁₃ in the _CHM from the top of the gas inlet of the pressure tank _{13 CHM,} sends the nitrogen is an inert gas. Chemical pressurized tank ₁₃ within _CHM is the pressure of nitrogen is pushed from the lower outlet of the pressure tank _{13 CHM.}

The pipe of the flow path 10 _CHM is connected to the inlet F2 of the mixing unit 50 _CHM . Chemicals are transferred to the flow path ₁₀ in the _CHM flows into from the inlet F2 to mixing unit _{50 CHM.}

FIG. 2A is a front view of the mixing unit 50 _CHM . FIG. 2B is a view of FIG. 2A as viewed in the direction of arrow B. FIG. 2 (C) is a view showing the inside of FIG. 2 (B). The mixing unit 50 _CHM comprises a housing HZ with two inlets F1 and F2 and one outlet F3 and a stirring screw SCR housed in the housing HZ. The main body of the housing HZ is a hollow cylindrical body having a diameter substantially the same as or slightly larger than the piping of the flow channel 10 _CHM or the flow channel 20 _DIW . One end of the main body of the housing HZ in the extending direction has an inlet F1 and the other end has an outlet F3. In the vicinity of the inlet F1 on the side of the main body of the housing HZ, there is an inlet F2. The inlet F2 is in communication with the main body of the housing HZ.

  The inlet F1 communicates with the pipe HK1 in the housing HZ. The tip of the pipe HK1 is connected to the stirring screw SCR. The inlet F2 communicates with the pipe HK2 in the housing HZ. At the end of the piping HK2, there is a nozzle NZ. The nozzle NZ is inserted into the pipe HK1 from the side of the pipe HK1. In the pipe HK1, the liquid discharge port of the nozzle NZ faces the stirring screw SCR.

  The stirring screw SCR arranges N (N is a natural number of 2 or more, N = 4 in the example of FIG. 2) twisted blades VL-k (k = 1 to N) at intervals on the shaft AXS. It is The shaft AXS is supported at the inlet F1 and the outlet F3 of the housing HZ. The torsion blade VL-k has a half-turn (180 degree) twist shape along the outer peripheral surface of the shaft rod AXS. The plurality of twisting blades VL-k (k = 1 to N) are arranged out of phase by 90 degrees, and the twisting blades VL-k which are adjacent to each other are orthogonally shifted by 90 degrees. The intervals of the torsion blades VL-k which are adjacent to each other are equal. The distance between the adjacent torsion blades VL-k is shorter than the dimension (the width in the front-rear direction) of the torsion blades VL-k itself.

Two liquid flowing from the mixing unit _{50 CHM} inlets F1 and inlet F2 in mixing unit ₅₀ in _CHM (ultrapure water and chemical) is mixed with each other while being agitated in the mixing unit _{50 CHM,} two liquid The liquid which prepared the above is sent out from the outlet F3 of mixing unit 50 _CHM .

The flow rate sensor 61 _CHM detects the flow rate per unit time of the liquid (ultrapure water) at a position immediately before the inlet F1 of the mixing unit 50 _CHM in the mixing flow path 40, and a signal SF1 _CHM indicating the detected flow rate Output. The flow rate sensor 62 _CHM detects the flow rate per unit time of the liquid (chemical) immediately before the inlet F2 of the mixing unit 50 _CHM in the preparation flow path 40, and outputs a signal SF2 _CHM indicating the detected flow rate . The flow rate sensor 63 _CHM detects the flow rate per unit time of the liquid immediately after the outlet F3 of the mixing unit 50 _CHM in the mixing flow path 40 (liquid prepared by mixing ultrapure water and chemicals), and the detected flow rate And outputs a signal SF3 _CHM indicating.

The flow path 10 _SLR is a circulation flow path returning from the flow path 10 _SLR to the drum 12 _SLR via the branch point 17 _SLR directed to the mixing flow path 40. The flow path 10 _SLR is provided with a pump 11 _SLR , a pressure tank 13 _SLR , a filling amount sensor 16 _SLR , a flow controller 15 _SLR , and a gas pressurizing unit 14 _SLR . The pump 11 _SLR pumps out the slurry in the drum 12 _SLR and supplies it to the side with the pressurized tank 13 _SLR in the flow path 10 _SLR . Slurry pumped by the pump _{11 SLR} flows into pressure tank _{13 SLR,} is filled into the pressure tank ₁₃ in the _SLR. An on-off valve VLU is provided at the liquid inlet of the upper part of the pressurized tank 13 _SLR , and an on-off valve VLL is provided at the liquid outlet of the lower part. The on-off valves VLU and VLL of the pressurized tank 13 _SLR open when the open signal SV _OP is given, and close when the close signal SV _CL is given.

The filling amount sensor 16 _SLR detects the filling amount of the slurry in the pressure tank 13 _SLR , and outputs a signal indicating the detected filling amount. Specifically, when the filling amount of the slurry in the pressure tank 13 _SLR falls below a predetermined value, the filling amount sensor 16 _SLR outputs a detection signal ST _SLR indicating that.

Gas pressure portion _{14 SLR} under the control of the flow controller _{15 SLR,} the pressure tank ₁₃ in the _SLR from the top of the gas inlet of the pressure tank _{13 SLR,} sends the nitrogen is an inert gas. The slurry of the pressure tank ₁₃ in the _SLR is the pressure of nitrogen is pushed from the lower outlet of the pressure tank _{13 SLR.}

The end of the flow path 10 _SLR piping that is branched from the branch point 17 _SLR is connected to the inlet F 2 of the mixing unit 50 _SLR . Slurry is transferred to the flow path ₁₀ in the _SLR, after branching at the branch point _{17 SLR,} it flows from the inflow port F2 in the mixing unit _{50 SLR.} The remaining slurry that did not advance to the side of the mixing unit 50 _SLR returns to the drum 12 _SLR through the piping between the branch point 17 _SLR and the drum 12 _SLR .

Mixing unit _{50 SLR} 2 kinds of liquid from the inlet F1 and F2 flowed into the mixing unit _{50 SLR} of (ultra-pure water and slurry containing chemicals), by passing through the stirring screw SCR of mixing unit _{50 SLR,} A liquid prepared by mixing while mixing and mixing chemicals, ultrapure water, and a slurry is delivered from the outlet F3 of the mixing unit 50 _SLR .

The structure of the mixing unit 50 _SLR is similar to that of the mixing unit 50 _CHM . As shown in FIGS. 2A, 2B and 2C, the mixing unit 50 _SLR has a housing HZ having two inlets F1 and F2 and one outlet F3. And a stirring screw SCR housed in the housing HZ.

Here, the liquid (ultrapure water containing chemical) flowing into the mixing unit 50 _SLR from the inflow port F1 and the liquid (slurry) flowing into the mixing unit 50 _SLR from the inflow port F2 are protrusions of the nozzle NZ in the piping HK1 Join at the same position. After this merging, the two types of liquid pass through the torsion blade VL-1 → the torsion blade VL-2 → the torsion blade VL-3 → the torsion blade VL-4 in order. As shown in FIG. 3A, each time the liquid passes through one torsion blade VL-k, the two types of liquid are added to the side of one torsion surface of the torsion blade VL-k and the other side of the torsion surface on the back side thereof. It is divided equally into the sides. Further, as shown in FIG. 3 (B), on the twisting surface of the torsion blade VL-k, the two types of liquids are from the side of the shaft rod AXS to the side of the inner wall surface, or from the side of the inner wall surface Reflux to the side of AXS, and so on. Furthermore, as shown in FIG. 3 (C), the rotational directions of the two types of liquid are reversed between the two torsion blades VL-k which are in succession. The three actions of the dividing action, the refluxing action, and the reversing action provide a solution in which the slurry is diluted to a uniform concentration.

In FIG. 1, the flow rate sensor 61 _SLR detects and detects the flow rate per unit time of the liquid (ultrapure water containing chemicals) at a position immediately before the inlet F1 of the mixing unit 50 _SLR in the mixing flow path 40 The signal SF1 _SLR indicating the flow rate is output. The flow rate sensor 62 _SLR detects the flow rate per unit time of the liquid (slurry) immediately before the inlet F2 of the mixing unit 50 _SLR in the mixing flow path 40, and outputs a signal SF2 _SLR indicating the detected flow rate. . The flow rate sensor 63 _SLR detects the flow rate per unit time of the liquid (ultrapure water, chemical, and slurry prepared liquid) at a position immediately after the outlet F3 of the mixing unit 50 _SLR in the preparation flow channel 40, A signal SF3 _SLR indicating the detected flow rate is output.

A pump 11 _{H 2 O 2} , a pressure tank 13 _{H 2 O 2} , a filling amount sensor 16 _{H 2 O 2} , a flow controller 15 _{H 2 O 2} , and a gas pressurizing unit 14 _{H 2 O 2} are provided in the flow passage 10 _{H 2 O 2} . The pump 11 _{H 2 O 2} pumps out the hydrogen peroxide solution in the drum 12 _{H 2 O 2} and supplies it to the side of the pressure tank 13 _{H 2 O 2} in the flow passage 10 _{H 2 O 2} . The hydrogen peroxide solution pumped out by the pump 11 _{H 2 O 2} flows into the pressure tank 13 _{H 2 O 2} and is filled in the pressure tank 13 _{H 2 O 2} . An on-off valve VLU is provided at the liquid inlet of the upper part of the pressurized tank 13 _{H 2 O 2} , and an on-off valve VLL is provided at the liquid outlet of the lower part. The on-off valves VLU and VLL of the pressurized tank 13 _{H 2 O 2} open when the open signal SV _OP is given, and close when the close signal SV _CL is given.

The filling amount sensor 16 _{H 2 O 2} detects the filling amount of the hydrogen peroxide solution in the pressure tank 13 _{H 2 O 2} , and outputs a signal indicating the detected filling amount. Specifically, when the filling amount of the hydrogen peroxide solution in the pressure tank 13 _{H 2 O 2} falls below a predetermined value, the filling amount sensor 16 _{H 2 O 2} outputs a detection signal ST _{H 2 O 2} indicating that.

The gas pressurizing unit 14 _{H 2 O 2 delivers} nitrogen, which is an inert gas, into the pressurized tank 13 _{H 2 O 2} from the gas inlet of the upper part of the pressurized tank 13 _{H 2 O 2} under control of the flow controller 15 _{H 2 O 2} . Hydrogen peroxide solution of the pressure tank ₁₃ in the _H2O2 is the pressure of nitrogen is pushed from the lower outlet of the pressure tank _{13 H2O2.}

The pipe of the flow path 10 _{H 2 O} 2 is connected to the inlet F ₂ of the mixing unit 50 _{H 2 O 2} . The hydrogen peroxide solution transferred in the flow path 10 _{H 2 O 2} flows into the mixing unit 50 _{H 2 O} 2 from the inlet F ₂ . The configuration of the mixing unit 50 _{H 2 O 2 is the same as} the configuration of the mixing unit 50 _CHM (FIG. 2).

Mixing unit 50 _{H2O2 from} the inlet F1 and the inlet F2 of the mixing unit 50 _{H2 O2} flowed into the mixing unit 50 _{H2 O2} is mixed while being stirred in the mixing unit 50 _{H2 O2} , mixing the liquid prepared two types of liquid, mixing It is sent out from the outlet F3 of the unit 50 _H2O2 .

The flow rate sensor 61 _{H 2 O 2} detects the flow rate per unit time of the liquid (ultrapure water, chemical, and slurry prepared liquid) at a position immediately before the inlet F 1 of the mixing unit 50 _{H 2 O 2} in the preparation flow channel 40, A signal SF1 _H2O2 indicating the detected flow rate is output. The flow rate sensor 62 _{H 2 O 2} detects the flow rate per unit time of the liquid (hydrogen peroxide water) at a position immediately before the inlet F ₂ of the mixing unit 50 _{H 2 O 2} in the preparation flow path 40, and indicates the detected flow rate signal SF _{2 H} 2 _{O 2} Output The flow rate sensor 63 _{H 2 O 2} is the liquid per unit time of the liquid immediately after the outlet F 3 of the mixing unit 50 _{H 2 O 2} in the preparation flow path 40 (ultrapure water, chemical, slurry, and liquid prepared with hydrogen peroxide solution). The flow rate is detected, and a signal SF3 _H2O2 indicating the detected flow rate is output.

The PLC 70 is a device that plays a role as a control unit of the polishing liquid supply device 2. PLC70 is mixing unit _{50 CHM} inlet F1 of the liquid pressure Pa, the mixing unit ₅₀ the pressure Pb of the hydraulic pressure Pb of the inlet F2 of _CHM, mixing unit _{50 SLR} inlet F1 of the liquid pressure Pc, mixing unit 50 _SLR pressure Pd of the liquid inlet F2 of mixing unit _{50 H2 O2} liquid pressure Pe inlet F1 of magnitude of the pressure Pf of the liquid inlet F2 of the mixing unit _{50 H2 O2} is, Pa <Pb <Pc < The first control of adjusting the gas pressure of the gas pressurizing units 14 _CHM , 14 _SLR , 14 _{H 2 O 2} by controlling the operation of the flow controllers 15 _CHM , 15 _SLR , 15 _{H 2 O 2} such that Pd <Pe <Pf. Flow control based on the relationship between the flow rate of the liquid in the The second control which controls the pressure of nitrogen of the gas pressurizing sections 14 _CHM , 14 _SLR and 14 _{H 2 O 2} by controlling the 14 _{CH M} , 15 _SLR and 15 _{H 2 O 2} ; And performing a third control of switching the communication.

More specifically described, PLC70, the flow sensor _{61 CHM,} 61 _{SLR, 61} and the output signal _{SF1 CHM, SF1 SLR, SF1 H2O2} of _{H2 O2,} the flow rate sensor _{62 CHM, 62 SLR, 62 H2O2} output signal _SF2 CHM, SF2 _The pressure Pa, Pb, Pc, Pd, Pe, Pd, Pf are monitored from _SLR , SF2 _H2O2 . The PLC 70 supplies the flow controller 15 _CHM with a signal SG indicating a pressure increase of the pressure of nitrogen when Pa ≧ Pb. The PLC 70 supplies, to the flow controller 61 _SLR , a signal SG instructing a pressure increase of nitrogen, when PcPcPd. The PLC 70 supplies the flow controller 15 _{H 2 O 2} with a signal SG instructing pressure increase of the pressure of nitrogen when PePePf.

PLC70, when the flow rate sensor ₆₁ value output signal _SF1 flow sensor _{62 SLR} output signal _{SF2 SLR} in _SLR divided the _SLR and current of dilution of the slurry, dilution of the slurry is lower than the target value of the dilution In addition, the flow controller 15 _SLR is supplied with a signal SG indicating an increase in pressure of nitrogen. The flow controller 15 _SLR controls the gas pressurizing unit 14 _SLR in accordance with the given signal SG to adjust the flow rate of the liquid in the flow path 10 _SLR .

The PLC 70 monitors the presence / absence of the output of the signals ST _CHM , ST _SLR and ST _{H 2 O 2} in the filling amount sensors 16 _CHM , 16 _SLR and 16 _{H 2 O 2} . The PLC 70 closes the on-off valves VLU and VLL of the pressurized tank 13 _CHM for which the filling amount is less than a predetermined amount for the four pressurized tanks 13 _CHM , and opens and closes the on-off valves VLU and VLL of the other pressurized tanks 13 _CHM. Repeat opening control repeatedly. The PLC 70 repeats the same control for the pressurized tanks 13 _SLR and 13 _{H 2 O 2} .

  The above is the details of the configuration of the present embodiment. According to the present embodiment, the following effects can be obtained.

  First, in the present embodiment, there is the mixing channel 40 communicating with the flow channel to which the ultrapure water, the chemical, the slurry, and the hydrogen peroxide solution are transferred, and in the mixing channel 40, plural kinds of liquids are The prepared and prepared liquid is supplied to the CMP polishing apparatus 8 as a polishing liquid. For this reason, in the present embodiment, it is not necessary to provide a preparation tank for preparing a plurality of types of liquids. Therefore, the liquid does not stay in the preparation tank to cause the generation of aggregation and precipitation, and the polishing solution having a uniform concentration can be stably supplied to the CMP polishing apparatus 8.

  Second, in the present embodiment, since there is no blending tank, installation of the drying prevention mechanism and the solidification preventing mechanism in the blending tank is also unnecessary. Along with this, replacement of expendables that play a part of the drying prevention mechanism and the solidification prevention mechanism is also unnecessary, so the number of maintenance steps of the polishing liquid supply device 2 can be significantly reduced.

  Thirdly, in the present embodiment, the preparation flow path 40 is disposed immediately before the liquid delivery port 79 leading to the CMP polishing apparatus 8. Therefore, after a plurality of types of liquids are mixed to obtain a polishing liquid, the polishing liquid can be used for polishing the wafer 88 of the CMP polishing apparatus 8 in a fresh state. Therefore, chemical attack is less likely to occur, and coarse particles that cause scratching can also be reduced. In addition, the polishing liquid does not change with time from preparation to use. Thereby, stable polishing characteristics can be obtained.

Fourth, in the present embodiment, the preparation channel 40, the mixing unit _{50 CHM, 50 SLR, 50 H2O2} is provided, the mixing unit _{50 CHM,} 50 _{SLR, 50} in _{H2 O2,} stirring screw SCR is provided The liquid flowing from the inlet is mixed while being stirred by passing the stirring screw SCR. Therefore, the time required for the stirring can be significantly reduced as compared with the conventional method in which the liquid is stored in the preparation tank and the stirring is performed by the stirring device. The mixing units 50 _CHM , 50 _SLR and 50 _{H 2 O 2} are less bulky than the blending tank, and the configurations of the mixing units 50 _CHM , 50 _SLR and 50 _{H 2 O 2} are simpler than the blending tank. Therefore, the device design of the CMP system 1 can be simplified, and the delivery time of the system can be shortened.

Fifth, in the present embodiment, in the mixing flow channel 40, the flow rate per unit time of the liquid in the mixing flow channel 40 is detected, and signals SF1 _CHM , SF1 _SLR , SF1 _H2O2, SF2 indicating the detected flow rates _There are flow sensors 61 _CHM , 62 _CHM , 63 _CHM , 61 _SLR , 62 _SLR , 63 _SLR , 61 _{H 2 O 2} , 62 _{H 2 O 2} , 63 _H 2 _{O 2} that output _CHM , SF2 _SLR , SF2 _H2O2 , chemical, slurry, hydrogen peroxide solution There are flow controllers 15 _CHM , 15 _SLR and 15 _{H 2 O 2} that adjust the flow rate of the liquid in the flow path according to the given signal SG in the flow path in which the is transferred. Then, a control unit PLC70, based on the relationship between the flow rate and the target value of the liquid in the preparation channel 40, and controls the operation of the flow controller _{15 CHM, 15 SLR, 15 H2O2} . Therefore, the slurry concentration can be efficiently adjusted by setting the target value of the flow rate with the operation element. In addition, it is possible to flexibly cope with a change in circumstances such as a change in the dilution ratio of the polishing liquid, a change in the wafer 88, and a change in the removal amount of polishing on the CMP polishing apparatus 8 side.

Sixth, in the present embodiment, the number of pressurized tanks 13 _CHM , 13 _SLR and 13 _{H 2 O 2} is plural (four each in the example of the present embodiment), and the PLC 70 serving as the control means below the metered dose pressurized tank _{13 CHM, 13 SLR, 13} closes the on-off valve VLU and VLL of _{H2 O2,} another pressure tank _{13 CHM, 13 SLR, 13} off valve _{H2 O2} VLU and control to open the VLL Repeat recursively. Therefore, according to the present embodiment, it is ensured that the liquid in the pressure tanks 13 _CHM , 13 _SLR and 13 _{H 2 O 2} is exhausted and the supply of the liquid to the mixing units 50 _{CH M} , 50 _SLR and 50 _{H 2 O 2} is interrupted. Can be prevented.

Second Embodiment
FIG. 4 is a view showing the overall configuration of a CMP system 1 including a polishing liquid supply apparatus 2 according to a second embodiment of the present invention. In FIG. 4, the same elements as those of the polishing liquid supply device 2 of the first embodiment are denoted by the same reference numerals. The mixing units 50 _CHM , 50 _SLR , and 50 _{H 2 O} 2 of the polishing liquid supply device 2 according to the first embodiment have a structure having a cylindrical body having a diameter substantially the same as or slightly larger than the flow path. Several liquids were in-line prepared in 50 _CHM , 50 _SLR , 50 _{H 2 O 2} . On the other hand, the mixing unit 50A of the polishing liquid supply device 2 of the present embodiment has a preparation tank 52A and a stirring device 59A, and a plurality of liquids are stirred and mixed in the tank 52A. ing.

The polishing liquid supply device 2 of the CMP system 1 includes a PLC 70A, an ultrapure water inlet 29 connected to an external ultrapure water supply source, a drum 12 _CHM in which a chemical is stored, and a drum 12 _SLR in which a slurry is stored. A drum 12 _{H 2 O 2} storing hydrogen peroxide solution, a flow passage 20 _DIW (second flow passage) forming a transfer passage of ultrapure water, a flow passage 10 A _CHM forming a transfer passage of a chemical, a transfer passage of slurry Flow path 10A _SLR (first flow path), flow path 10A _H2O2 which forms a transfer path of hydrogen peroxide solution, and mixing unit 50A connected to the flow path of these flow paths 10A _CHM , 10A _SLR , 10A _H2O2. The flow path 40A from the mixing unit 50A to the CMP polishing apparatus 8 is provided.

The flow path 10A _CHM is provided with a pump 11 _CHM . The pump 11 _CHM pumps out the chemical in the drum 12 _CHM and supplies it to the side of the mixing unit 50A in the flow path 10A _CHM . Pump 11 _SLR is provided in flow path A10 _SLR . The pump 11 _SLR pumps out the slurry in the drum 12 _SLR and supplies it to one side of the mixing unit 50A in the flow path 10A _SLR . A pump 11 _{H 2 O 2} is provided in the flow path 10 A _{H 2 O 2} . The pump 11 _{H 2 O 2} pumps out the hydrogen peroxide solution in the drum 12 _{H 2 O 2} and supplies it to the side of the mixing unit 50 A in the flow path 10 A _{H 2 O 2} .

  The flow path 40A is a circulation flow path returning to the mixing tank 52A of the mixing unit 50A via the branch point 17A directed to the CMP polishing apparatus 8.

  The mixing unit 50A prepares a polishing liquid used for polishing the CMP polishing apparatus 8 by preparing four types of liquids, chemical, ultrapure water, slurry, and hydrogen peroxide water. The mixing unit 50A includes a housing 51A, a preparation tank 52A, a stirring device 59A, a pressure tank 13A, a filling amount sensor 16A, a flow controller 15A, and a gas pressurizing unit 14A.

  The housing 51A has a hollow rectangular parallelepiped shape. At the upper part in the housing 51A, there is a preparation tank 52A, and at the lower part in the housing 51A, there are a plurality (three in the example of FIG. 2) of pressurized tanks 13A.

The blending tank 52A has a hollow cylindrical shape. Flow path 20 _DIW transferred ultrapure water, flow path 10A _CHM transferred chemical, flow path 10A _SLR transferred slurry, flow path 10A _H2O2 transferred hydrogen peroxide solution, blending tank 52A Flow into The stirring device 59A stirs and mixes the four types of liquid flowing into the mixing tank 52A.

  At the bottom of the blending tank 52A, there is a pipe extending downward. The pipe is branched into a plurality of pipes, and the branched pipe is connected to the inlets of the plurality of pressure tanks 13A. The pressure tank 13A has a cylindrical shape. The pressurizing tank 13A is disposed at a position directly below the preparation tank 52A in the housing 51A, with the inlet facing upward and the outlet facing downward.

The polishing liquid obtained by stirring the four types of liquid in the preparation tank 52A flows into the pressure tank 13A through the lower pipe by its own weight, and is filled in the pressure tank 13A. An on-off valve VLU is provided at the liquid inlet of the pressurized tank 13A, and an on-off valve VLL is provided at the liquid outlet. The on-off valves VLU and VLL of the pressurization tank 13A open when the open signal SV _OP is given, and close when the close signal SV _CL is given.

  The filling amount sensor 16A detects the filling amount of the liquid in the pressure tank 13A, and outputs a signal indicating the detected filling amount. Specifically, when the filling amount of the liquid in the pressurizing tank 13A falls below a predetermined value, the filling amount sensor 16A outputs a detection signal ST indicating that.

  The gas pressurizing unit 14A delivers nitrogen, which is an inert gas, from the gas inlet at the top of the pressure tank 13A into the pressure tank 13A under the control of the flow controller 15A. The liquid in the pressure tank 13A is pushed out from the outlet of the lower part of the pressure tank 13A by the pressure of nitrogen.

  The PLC 70 </ b> A is a device that plays a role as a control unit of the polishing liquid supply device 2. PLC70A performs control which switches what is connected with the preparation flow path 40 among the pressurization tanks 13A.

  More specifically, the presence or absence of the output of the signal ST in the filling amount sensor 16A is monitored. The PLC 70A closes the on-off valves VLU and VLL of the pressurized tank 13A for which the filling amount is less than a predetermined amount for the three pressurized tanks 13A and opens the on-off valves VLU and VLL of another pressurized tank 13A. Repeat control recursively.

The above is the details of the configuration of the present embodiment. According to the present embodiment, the following effects can be obtained.
First, in the present embodiment, the polishing liquid obtained by the preparation of the liquid in the preparation tank 52A of the mixing unit 50A is filled in the pressurization tank 13A, and the gas pressurization unit 14A is not contained in the pressurization tank 13A. The active gas is delivered to push the polishing solution in the pressure tank 13A to the path to the CMP polishing apparatus 8. Therefore, it is possible to stably supply the CMP polishing apparatus 8 with an ultra-high-precision polishing liquid without pulsation.

  Second, in the present embodiment, the preparation tank 52A for storing the polishing liquid obtained by the preparation of the liquid is provided, and the flow path leading to the CMP polishing apparatus 8 is branched from the preparation tank 52A toward the CMP polishing apparatus 8. It becomes a circulation flow path which returns to the preparation tank 52A via point 17A. Therefore, the liquid does not stay in the preparation tank 52A and the occurrence of aggregation and precipitation is prevented, and the polishing liquid having a uniform concentration can be stably supplied to the CMP polishing apparatus 8.

  Third, in the present embodiment, the pressure tank 13A is disposed below the mixing tank 52A so that the liquid flows from the mixing tank 52A into the pressure tank 13A by the weight of the liquid in the mixing tank 52A. It has become. Therefore, it is not necessary to provide a special device such as a pump in the mixing tank 52A, and the liquid can be transferred from the mixing tank 52A to the pressure tank 13A without the risk of oxidation of the polishing liquid or change in composition.

  Fourthly, in the present embodiment, the pressure tank 13A has a cylindrical shape, and the pressure tank 13A has the liquid inlet from the mixing tank 52A to the pressure tank 13A at the top, and the pressure tank The liquid outlet from 13 A to the CMP polishing apparatus 8 is disposed at the bottom. Accordingly, the flow of the liquid, that is, the preparation tank 52A → the pressure tank 13A → the CMP polishing apparatus 8 can be made smoother.

  Fifth, in the present embodiment, the number of pressurized tanks 13A is plural, and the PLC 70 serving as the control means closes the on-off valves VLU and VLL of the pressurized tank 13A whose filling amount is less than a predetermined amount, The control of opening the on-off valves VLU and VLL of another pressurized tank 13A is recursively repeated. Therefore, according to the present embodiment, it is possible to reliably prevent the occurrence of a situation where the liquid in the pressure tank 13A is exhausted and the supply of the liquid to the CMP polishing apparatus 8 is interrupted.

<Modification>
Although the first and second embodiments of the present invention have been described above, the following modifications may be added to these embodiments.

(1) In the first embodiment, the flow sensors 61 _CHM , 61 _SLR , 61 _H2O2, 62 _CHM , 62 _SLR , 62 _{H2 O2} detect the flow rate per unit time of the liquid in the mixing channel 40, and the flow controller The 15 _CHM , 15 _SLR and 15 _{H 2 O 2} were designed to adjust the flow rate of the liquid in the flow channels 61 _CHM , 61 _SLR and 61 _{H 2 O 2} according to the given signals. However, the flow sensors 61 _CHM , 61 _SLR , 61 _H2O2, 62 _CHM , 62 _SLR , 62 _H2O2 detect the pressure of the liquid in the mixing channel 40, and the flow controllers 15 _CHM , 15 _SLR , 15 _{H2 O2} are The pressure of the liquid in the channels 61 _CHM , 61 _SLR and 61 _{H 2 O 2} may be adjusted according to the signal.

(2) The order of preparation of the plurality of types of liquids in the preparation flow channel 40 of the first embodiment is not limited to that of the first embodiment. For example, the slurry and the chemical may be prepared first, then the hydrogen peroxide solution may be prepared, and finally the ultrapure water may be prepared and diluted.

(3) The number of each of the pressure tanks 13 _CHM , 13 _SLR and 13 _{H 2 O 2} in the first embodiment may be two to three, or five or more. Further, the number of pressure tanks 13A in the second embodiment may be two, or four or more.

(4) In the first embodiment, the pressure tank _{13 CHM,} 13 _{SLR, 13 H2O2,} nitrogen delivery, pressurized tank _{13 CHM,} 13 _{SLR, 13} liquid in the _H2O2 is, by the pressure of nitrogen, pressurized The pressure tanks 13 _CHM , 13 _SLR and 13 _{H 2 O 2} were pushed out. However, another inert gas (e.g., argon) may be delivered to the pressure tanks 13 _CHM , 13 _SLR , 13 _{H 2 O 2} .

(5) In the second embodiment, nitrogen is delivered to the pressure tank 13A, and the liquid in the pressure tank 13A is pushed out of the pressure tank 13A by the pressure of nitrogen. However, another inert gas (for example, argon) may be delivered to the pressure tank 13A.

(6) In the first embodiment, it is not necessary for both the inlet and outlet of the pressurized tanks 13 _CHM , 13 _SLR and 13 _{H 2 O 2} to be provided with an on-off valve. The on-off valve may be provided on at least one of the inlet and the outlet of the pressurized tanks 13 _CHM , 13 _SLR , and 13 _{H 2 O 2} , and the PLC 70 serving as the control means repeats the control to open and close the on-off valve recursively. You may do so.

(7) In the second embodiment, it is not necessary for both the inlet and outlet of the pressurized tank 13A to be provided with the on-off valve. An open / close valve may be provided on at least one of the inlet and the outlet of the pressurized tank 13A, and the control by the PLC 70A as the control means may repeat the control of opening and closing the open / close valve recursively.

(8) In the first embodiment, the mixing units 50 _CHM , 50 _SLR , and 50 _{H 2 O 2} contain the stirring screw SCR in a cylindrical body, and the stirring screw SCR includes N torsion blades on the shaft AXS. VL-k (k = 1 to N) was disposed at intervals. However, as in the mixing units 50 ′ _CHM , 50 ′ _CSLR , 50 ′ _{H 2 O 2} shown in FIGS. 5A and 5B, in the hollow cylinder extending between the inlet F 1 and the outlet F 3, The direction of the mesh mesh of the mesh VL′-k is one in which N (N is a natural number of 2 or more, N = 4 in the example of FIG. 5) meshes VL′-k (k = 1 to N) The stirring screw SCR may be replaced by a mixer arranged so as to be shifted in a predetermined angle (45 degrees in the example of FIG. 5B).

(9) In the first and second embodiment, pressure tank _{13 CHM, 13 SLR, 13 H2O2} , 13A has the inlet of the liquid at the top of pressure tank _{13 CHM, 13 SLR, 13 H2O2} , 13A of There was a liquid outlet at the bottom. However, both liquid inlets and outlets may be provided below the pressurized tanks 13 _CHM , 13 _SLR , 13 _{H 2 O 2} and 13 _A. For example, as shown in FIG. 6, a pipe is provided at the bottom (bottom) of 13 _CHM , 13 _SLR , 13 _{H 2 O 2} and 13 A, and the lower part of this pipe is branched into a T shape on the inflow side and the outflow side of the liquid. In addition to providing the first valve VAL1 in the inflow side piping, the second valve VAL2 may be provided in the outflow side piping. Then, until the filling amount of the pressurized tank 13 _CHM , 13 _SLR , 13 _{H 2 O 2} , 13 A reaches a predetermined amount (for example, 90%), the PLC opens the first valve VAL 1 and closes the second valve VAL 1 Te, Once pressurized tank _{13 CHM, 13 SLR, 13 H2O2} , 13A in the liquid is filled into the pressurized tank _{13 CHM, 13 SLR, 13 H2O2} , loading of 13A of the liquid reaches a predetermined amount, the first valve The control of closing the valve VAL1 and opening the second valve VAL1, and pushing out the liquid in the pressurized tanks 13 _CHM , 13 _SLR , 13 _{H 2 O 2} and 13 A by the pressure of nitrogen may be repeated repeatedly.

(10) In the first embodiment, the channel 10 _CHM is connected to the inlet F2 of the mixing unit 50 _CHM , the channel 10 _SLR is connected to the inlet F2 of the mixing unit 50 _SLR , and the channel 10 _H2O2 is the mixing unit 50. It was configured to be connected to the _{H 2 O 2} inlet F ₂ . However, as shown in FIG. 7, the channel 10 _CHM is connected to the inlet F1 of the mixing unit 50 _CHM , the channel 10 _SLR is connected to the inlet F1 of the mixing unit 50 _SLR , and the channel 10 _H2O2 is the mixing unit 50 _{H2 O2} It may be connected to the inflow port F1.

14A Gas pressurizing unit 15A Flow controller 16A Filling amount sensor 17A Bifurcation point 21 Low pressure valve 29 Ultra pure water inlet / outlet 40 Blending flow path 40A Flow path 50A Mixing unit 51A Housing 52A Mixing tank 59A Stirring device 70 PLC
79 liquid delivery port 81 head 82 board 83 base 84 polishing pad 85 nozzle 88 wafer 89 liquid feed port 91 tank 92 pump

Claims (1)

A polishing liquid supply apparatus for supplying a polishing liquid to a CMP polishing apparatus, comprising:
A first flow path for transferring the slurry;
A second flow path for transferring pure water,
A plurality of mixing channels disposed immediately before the liquid delivery port leading to the CMP polishing apparatus, the plurality including the slurry and the pure water in communication with the first channel and the second channel. A preparation flow path for supplying a liquid prepared by mixing various types of liquids to the CMP polishing apparatus as the polishing liquid;
Control means,
A sensor provided in the mixing channel, which detects the flow or pressure of the liquid in the mixing channel, and outputs a signal indicating the detected flow or pressure;
A flow controller provided in the first flow path, the flow controller adjusting the flow rate or pressure of the liquid in the first flow path according to a given signal;
The control means
The operation of the flow controller is controlled based on the relationship between the flow rate of the liquid in the mixing channel and the target value ,
The mixing channel is provided with a mixing unit for mixing a plurality of types of liquids including the slurry and the pure water,
The mixing unit has a first inlet at one end of a hollow cylindrical housing, an outlet at the other end of the cylindrical housing, and A second inlet is provided on the side, and a stirring screw is provided in the cylindrical housing.
The liquid flowing from the first inlet and the second inlet is configured to be mixed while being stirred by passing through the stirring screw,
The stirring screw is a shaft in which N (N is a natural number of 2 or more) twisting blades VL-k (k = 1 to N) are disposed with a phase shift of 90 degrees each, and a twisting blade is Each of VL-k (k = 1 to N) has a shape that is twisted by a half rotation along the outer peripheral surface of the shaft,
The first inlet is in communication with a first pipe in the housing, the tip of the first pipe is connected to the agitating screw, and the second inlet is a second pipe in the housing In communication, there is a nozzle at the end of the second pipe, and the nozzle is inserted into the first pipe from the side of the first pipe, and in the first pipe, the nozzle is A polishing liquid supply apparatus characterized in that a liquid discharge port faces the stirring screw .