In manufacturing electronic products, thousands of individual microelectronic devices are generally formed on a single semiconductor wafer or another type of substrate. In a typical fabrication process, one or more thin metal layers are formed on a substrate at various stages of fabricating the microelectronic devices. The metal layers are often applied to the substrate in an electroplating chamber. A typical electroplating chamber includes a bowl or vessel for holding an electroplating solution, one or more anodes in the vessel in contact the electroplating solution, and a substrate holder having a contact ring with multiple electrical contacts that engage a seed-layer on a front surface the substrate. The electrical contacts are coupled to a power supply to apply a voltage to the seed layer. In operation, the front surface of the substrate is immersed in the electroplating solution so that the anode and the seed layer establish an electrical field that causes metal ions in the electroplating solution to plate out onto the seed layer.
As feature sizes continue to shrink, the metal seed layer used to initiate the electroplating process must also be thinner as well. As the seed layer gets thinner it becomes more important that the electrical contacts touching the seed layer are clean and dry. Liquid remaining on the contacts and touching the seed layer has the potential to etch the seed layer. An etched seed layer causes the loss of electrical contact in the etched location which results in an unacceptable electroplated wafer.
In electroplating processors where the contacts are exposed to the plating bath, metal is plated onto the seed layer, and also onto the contacts. The contacts must be frequently “de-plated” to remove the metal that plates onto them. Techniques for deplating contacts have been known and used in the past with varying degrees of success. Still, engineering challenges remain in the design of deplating features in electroplating chambers capable of plating onto ever thinner seed layers.
An electroplating chamber de-plates, rinses and dries a ring contact. This reduces consumption of deplating liquid, and more effectively captures or confines overspray and out gassing during the de-plate, rinse and dry processes.
As shown in
Contacts on a contact ring 40 make electrical contact with a seed layer on the substrate. Electrical current flows through the plating liquid, the contacts and the seed layer, causing metal ions in the plating liquid to deposit out onto the seed layer, resulting in a plated metal layer on the seed layer.
The contacts on the contact ring 40 may be deplated by positioning the contact ring 40 into a deplate station 50, as shown in
As shown in
Referring to
The deplate housing 60 may include similar fittings or connections for ring backside deplate liquid lead-in 80, ring exhaust/vacuum 82, exterior rinse 74, contact rinse 72, contact drying gas 68, backside exhaust 82, and ring exhaust 66. A contact rinse nozzle 90 on a bottom surface of the deplate housing 60 is supplied with rinse liquid from contact rinse line 72, and is positioned to jet or spray rinse liquid radially outwardly, or outwardly at an acute angle, onto contacts on the contact ring 40. Similarly, a contact dry nozzle 92 is positioned to spray drying gas from drying gas line 64 onto the contacts.
Especially for use in plating thin seed layers, the contact ring 40 may have large number, e.g., 720 narrow contacts 114. It has been discovered that to obtain the very high level of clean required to consistently electroplate thin metal seed layers, applying deplating liquid only to the contacts themselves may not be sufficient. Accordingly, the deplate station 50 also includes elements directed to deplating the back side 112 of the contact ring 40. Turning to
In use, the actuator 54 moves the deplate head 52 into the open position. The lift/rotate assembly moves the head to place the contact ring 40 into the deplate channel 58. In some processors 20, the contact ring 40 may also be extended outwardly from the head during this step. With a sector of the contact ring 40 in the deplate channel 58, the head 22 slowly rotates the rotor and the contact ring 40, continuously and sequentially moving the contacts 114 through the deplate channel 58. Deplate liquid is supplied to the contact nozzle 90. At the same time, reverse current is applied to the contact deplate electrode 76. The deplate liquid jetting or spraying out of the nozzle 90 impinges on the ring lead-in 110, passes over and between the contacts 114, through the rinse holes 116 and is exhausted or vacuumed out through the exhaust channel 118.
In addition, deplate liquid is similarly applied to the back side 112 of the contact ring 40 from the ring deplate nozzle 100 and drawn off via the exhaust opening 122, while reverse or deplating current is applied to the ring deplate electrode 98. The exhaust seal 122 makes sliding resilient contact with the back side of the contact ring. The exhaust opening 122 consequently is able to positively draw or pull liquid through the openings in the contact ring 40. Accordingly, even though the openings in the contact ring may be very small, typically in the range of 0.02 to 0.1 mm, capillary and other forces are overcome and the liquid is caused to effectively flow through the openings.
Depending on factors such and the chemical make up of plating bath, the seed layer thickness, and others, the contact ring 40 may be deplated in a single rotation, although a second or more deplate rotations may be used if necessary. After the deplate rotation, rinse liquid is applied to the contacts 114 and the back side 112 of the contact ring 40, in the same way as the deplate liquid, although no electrical current need by applied to the deplate electrodes 76 and 98.
The rinse liquid is advantageously supplied through the same channels in the deplate station 50 as used for the deplate liquid. Alternatively, separate rinse liquid channels may be used. The rinse step typically is carried out over one or two rotations of the contact ring 40, although additional rinse rotations may be used.
The contacts 114 are then dried via a spray or jet of a drying gas directed at the contacts from the contact dry nozzle 92. The back side of the contact ring 40 is simultaneously dried by airflow movement drawn into the seal exhaust opening 122. The drying gas may be clean dry air, or another gas. The drying gas may optionally be applied from the same nozzles and openings as used to apply the deplate liquid, and/or the rinse liquid. With this option, dripping can be largely avoided because the drying gas purges the liquid out from the supply lines and nozzles or openings. Alternatively, the drying gas may be applied from separate lines and nozzles.
As shown in
The ring maintenance station pivots over the contact ring 40 after the contact ring 40 is moved into the deplate position shown in
As shown in
With the design described, de-plate, rinse and dry steps may be achieved with substantially less fluid consumption compared to existing designs. Another advantage is that only relatively small volumes of liquid pass through the ring. This provides for fast fluid exchange as well as a reduced fluid consumption, and with rapid drying. Since deplating occurs away from the plating bath, chemicals or gasses may be used without contaminating the process bath. In use, the maintenance station 50 also largely encloses the contact ring 40. This helps contain particles and spatter that result from the deplate, rinse and dry steps. The station may be efficient enough that a deplate, rinse and dry can each be accomplished in one rotation.
This application claims priority to U.S. Provisional Application No. 61/706,256, filed Sep. 27, 2012, and now pending.
Number | Date | Country | |
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61706256 | Sep 2012 | US |