Method and apparatus for dry/catalytic-wet steam oxidation of silicon

Abstract

A configuration of various chemical compound generators coupled to a furnace provides the environment for formation of extremely thin oxides of silicon on a wafer. Dichloroethylene is reacted with oxygen in a first heated reaction chamber and reaction products therefrom are diluted with a gas such as nitrogen and then introduced into a vertically oriented furnace maintained at an elevated temperature and having rotating wafers therein. Hydrogen and oxygen are catalytically reacted to form steam in a second heated reaction chamber, the steam is diluted with a gas such as nitrogen and introduced into the vertical diffusion furnace. In a further aspect of the present invention, MOSFETs having gate dielectric layers of extremely thin oxides of silicon are formed.

Description

BACKGROUND OF THE INVENTION

[0001] 1. Field of the Invention

[0002] The present invention relates generally to semiconductor structures and manufacturing. More particularly, the invention relates to extremely thin dielectric layers and the methods and apparatus for the formation thereof.

[0003] 2. Background

[0004] Advances in semiconductor manufacturing technology have led to the integration of millions of circuit elements, such as transistors, on a single integrated circuit (IC). In order to integrate increasing numbers of circuit elements onto an integrated circuit it has been necessary to reduce the line widths of the various parts that make up an integrated circuit. Not only have interconnect line widths become smaller, but so have the dimensions of metal-oxide-semiconductor field effect transistors (MOSFETs).

[0005] MOSFETs are also sometimes referred to as insulated gate field effect transistors (IGFETs). Most commonly, these devices are referred to simply as FETs, and are so referred to in this disclosure.

[0006] Transistor scaling typically involves more than just the linear reduction of the FET width and length. For example, both source/drain (S/D) junction depth and gate dielectric thickness are also typically reduced in order to produce a FET with the desired electrical characteristics.

[0007] Over the years, a substantial amount of research and development in the field semiconductor manufacturing has been dedicated to providing reduced thickness dielectric layers, as mentioned above. However, to be suitable for use as a MOSFET gate dielectric layer, these reduced thickness dielectric layers are typically required to provide certain electrical characteristics. For example, the dielectric layer should have a low density of interface states, a low density of defects, and a dielectric breakdown voltage high enough for use with the desired voltages that the MOSFET will encounter during operation. Furthermore, such a reduced thickness dielectric layer should be manufacturable with great uniformity and repeatability.

[0008] What is needed is an extremely thin dielectric layer suitable for use as the gate dielectric layer in a MOSFET, and what is further needed are apparatus and methods for repeatably making such ultra-thin dielectric layers.

SUMMARY OF THE INVENTION

[0009] Briefly, a configuration of various chemical compound generators coupled to a furnace provides the environment suitable for repeatably forming extremely thin oxides of silicon on a wafer with a high degree of uniformity.

[0010] In a further aspect of the present invention, MOSFETs having gate dielectric layers of extremely thin oxides of silicon are formed.

BRIEF DESCRIPTION OF THE DRAWINGS

[0011] FIG. 1 is a schematic representation of a furnace and associated chemical compound generators coupled thereto in accordance with the present invention.

[0012] FIG. 2 is a flow diagram of a process in accordance with the present invention.

[0013] FIG. 3 is a flow diagram of a process in accordance with the present invention.

DETAILED DESCRIPTION

[0014] Terminology

[0015] The terms, chip, integrated circuit, monolithic device, semiconductor device or component, microelectronic device or component, and similar terms and expressions are often used interchangeably in this field. The present invention is applicable to all the above as they are generally understood in the field.

[0016] Historically, the material most commonly used in the semiconductor industry to form the gate insulator layer of a FET is silicon dioxide. Thus, the gate insulator layer is frequently referred to simply as the gate oxide. The expression gate dielectric is also used to describe the gate insulator layer.

[0017] The term “gate” is context sensitive and can be used in two ways when describing integrated circuits. Gate refers to a circuit for realizing an arbitrary logical function when used in the context of a logic gate. However, as used herein, gate refers to the insulated gate terminal of a three terminal FET when used in the context of transistor circuit configurations or formation of transistor structures. The expression “gate terminal” is generally interchangeable with the expression “gate electrode”. A FET can be viewed as a four terminal device when the semiconductor body is considered, for the purpose of describing illustrative embodiments of the present invention, the FET will be described using the traditional gate-drain-source, three terminal model.

[0018] Polycrystalline silicon is a nonporous form of silicon often formed by chemical vapor deposition from a silicon source gas, or other methods, and has a structure that contains crystallites or domains with large-angle grain boundaries, twin boundaries, or both. Polycrystalline silicon is often referred to in this field as polysilicon, or sometimes more simply as poly.

[0019] Source/drain terminals refer to the terminals of a FET, between which conduction occurs under the influence of an electric field, subsequent to the inversion of the semiconductor surface under the influence of a vertical electric field resulting from a voltage applied to the gate terminal. Generally, the source and drain terminals are fabricated such that they are geometrically symmetrical. With geometrically symmetrical source and drain terminals it is common to simply refer to these terminals as source/drain terminals, and this nomenclature is used herein. Designers often designate a particular source/drain terminal to be a “source” or a “drain” on the basis of the voltage to be applied to that terminal when the FET is operated in a circuit.

[0020] Overview

[0021] An arrangement of equipment, and methods of operation are disclosed for the formation of extremely thin oxides of silicon on a wafer. These oxides are formed with a high degree of uniformity both within wafer and wafer-to-wafer, and are electrically suitable for use as a gate dielectric layer.

[0022] In accordance with the present invention, a configuration of equipment for forming extremely thin oxides of silicon with excellent uniformity, both within wafer, and wafer-to-wafer, includes a first heated reaction chamber coupled to an O2 source and a 1,2-dichloroethylene (DCE) source, such as, for example, a bubbler. The first reaction chamber has an output port coupled through a first pathway to a showerhead arrangement of a furnace. The first pathway is also coupled to a source of a diluting gas, such as, for example, nitrogen. A second heated reaction chamber having a metal catalyst therein is coupled to an O2 source, an H2 source, and an N2 source. The second reaction chamber has an output port coupled to the showerhead arrangement of a furnace. The furnace is typically vertically oriented. In this orientation, the showerhead is typically at the top end of the furnace. The bottom end of the furnace typically has an opening through which it receives a container of wafers. Such a furnace is sometimes referred to in this industry as a vertical diffusion furnace (VDF) regardless of whether it is used for a diffusion operation or some other high temperature operation.

[0023] A method of forming a dielectric having a thickness of approximately 10 angstroms (1.0 nm) or less on a silicon substrate includes placing wafers into a furnace and performing a dry chlorinated oxidation operation, and a wet oxidation with steam. The wafers are rotated at approximately 3 rpm during the dry and wet oxidations and the furnace is maintained at approximately 625° C. In accordance with the present invention, both the dry and wet oxidation operations require the preparation of gases external to the furnace. In one reaction chamber, a reaction of 1,2-dichloroethylene and oxygen at elevated temperatures produces, primarily, HCl and CO2, which together with other reaction products, O2, and N2, are passed to the showerhead of the furnace to begin the dry oxidation operation. In another reaction chamber, H2 and O2 are catalytically combined to form steam. The steam, together with nitrogen, is passed to the showerhead of the furnace to begin the wet oxidation operation. In this way, a dry/catalytic steam oxidation is accomplished.

[0024] Oxide Furnace Example

[0025] A first illustrative embodiment of the present invention is described below in connection with FIG. 1. As shown in FIG. 1, a vertically oriented furnace 102 has a showerhead arrangement 104, or more simply showerhead 104, at a top portion thereof so as to enable the introduction of various gases into furnace 102. A push mechanism 106 is used to push a wafer container 108 into furnace 102, and to move wafer container 108 back out again. Push mechanism 106 is adapted so that it may provide a rotational velocity to wafer container 108. Showerhead 104 is coupled to input plumbing 110. Input plumbing 110, in turn, is coupled to stainless steel plumbing 126, and to plumbing 114. Plumbing 114 is coupled to a diluting gas source 117 through plumbing 116. Plumbing 114 is further coupled to reaction chamber 112. Reaction chamber 112 is coupled to a 1,2-dichloroethylene (DCE) source 118, and an O2 source 122. DCE source 118, in the illustrative embodiment of FIG. 1, is a bubbler which is further coupled to receive an N2 carrier gas via plumbing 120. Stainless steel plumbing 126, which is adapted to maintain a particular temperature range, is coupled to reaction chamber 124. Reaction chamber 124 is coupled to H2 source 128, O2 source 130, and N2 source 132. Those skilled in the art and having the benefit of this disclosure will appreciate that plumbing as used herein may be implemented as tubing, and that such tubing may be made from any of various materials suitable for the gases and temperatures used.

[0026] Reaction chamber 112 is adapted to receive DCE and O2 and heat these gases. Reaction products such as HCl and CO2, as well as unreacted O2 exit reaction chamber 112 through plumbing 114. This stream of gases is then combined with at least one other gas in order to dilute the gases exiting from reaction chamber 112. In one embodiment of the present invention, N2 is used to achieve this dilution. In this context, N2 is referred to herein as a diluting gas.

[0027] Reaction chamber 124 is adapted to receive H2 and O2, and catalytically combine the H2 and O2 to produce steam. Reaction chamber 124 is further adapted to receive a diluting gas, in this case N2. Additionally, reaction chamber 124 is adapted to couple the steam to plumbing 126. An H2 detector may be coupled to the output of reaction chamber 124. The H2 detector may be coupled to an alarm such that when a predetermined amount of H2 is detected an alarm is activated which notifies one or more operators, or may alternatively notify other equipment, that an unacceptable level of H2 is contained in the gases which exit reaction chamber 124.

[0028] Furnace 102 is adapted to heat the wafers and gases introduced thereinto, and to maintain a particular temperature or temperature gradient. As indicated above, wafers 109 are introduced into furnace 102 by push mechanism 106 which delivers wafer container 108 into furnace 102. A furnace controller 150 is coupled to furnace 102 and push mechanism 106 and provides the control signals for setting and maintaining various temperatures for programmed times, as well as for providing control signals to push mechanism 106 which determine push rates, pull rates, and rotation speeds. Furnace controllers are well-known in this field and not described in further detail hereafter.

[0029] Oxide Formation Example

[0030] A first exemplary process for the formation of an oxide of silicon suitable for use as a MOSFET gate dielectric is described in conjunction with FIG. 2.

[0031] In this illustrative embodiment of the present invention, prior to beginning the dry and wet oxidation operations, the wafers are loaded in a wafer container, sometimes referred to as a boat, the boat is placed into a load lock chamber of the furnace, the load lock door is closed, the chamber is evacuated and purged with N2. The boat is then pushed into the furnace tube with a 0.1 slpm O2 flow and 9.9 slpm N2 flow. The furnace temperature is then ramped up from approximately 500° C. to approximately 625° C. with a gas mixture flow of 0.1 slpm O2, and 9.9 slpm N2. Pushing the wafers into the furnace under these conditions forms a first amount of oxide on the surface of the wafers. This oxide is sometimes referred to as a push oxide because it forms while the wafers are being pushed into the furnace. The container of wafers is pushed into a vertically oriented furnace. Such a wafer container typically contains approximately 125 silicon wafers, with each wafer typically having a diameter of 200 mm (sometimes referred to in this field as eight inch wafers). Those skilled in the art will recognize that other wafer sizes, or a different number of wafers may be used with embodiments of the present invention. The wafer container is pushed into the furnace at a rate of approximately 500 mm per minute with the furnace at approximately 500° C., and a gas flow into the furnace of 0.1 slpm O2, and 9.9 slpm N2 being provided. The furnace temperature is then ramped up from 500° C. to 625° C., and a gas mixture flow of 0.1 slpm O2, and 9.9 slpm N2 is provided.

[0032] As shown in FIG. 2, in accordance with the present invention, the 200 mm wafers are rotated, and in this exemplary embodiment given a rotational velocity of approximately 3 rpm, and their temperature is maintained at approximately 625° C. (block 202). It is preferable to maintain temperature control of the furnace such that the gradient is less than or equal to 2° C. from one end of the furnace to the other. A first gas mixture including HCl, CO2, and O2, diluted with nitrogen is provided to the furnace from a showerhead arrangement at the top of the vertically-oriented furnace (block 204). This operational phase is referred to as a dry oxidation. The dry oxidation takes place for approximately 2 minutes. The wafers are rotated and maintained at this temperature, i.e., 625° C., with the first gas mixture provided at atmospheric pressure for a period of approximately 2 minutes, as mentioned above. The first gas mixture is obtained from the reaction of 1,2-dichloroethylene and oxygen at approximately 800° C. The 1,2-dichloroethylene is typically provided to a reaction chamber, in which it is combined with oxygen, from a bubbler using nitrogen as a carrier gas. HCl, and CO2, are produced during this reaction. Nitrogen is fed through the bubbler at approximately 0.29 slpm, and O2 is fed to the reaction chamber at approximately 2.71 slpm. The reaction products are combined with molecular nitrogen to dilute their concentration and piped to the showerhead of the furnace. The diluting nitrogen is supplied at a flow rate of approximately 20 slpm.

[0033] Still referring to FIG. 2, a second gas mixture is provided to the furnace (block 206). This second gas mixture is formed by the catalytic reaction of hydrogen and oxygen in the presence of nitrogen at approximately 500° C. Hydrogen is supplied to the catalytic reaction chamber at the rate of approximately 0.5 slpm, oxygen is supplied at the rate of approximately 0.98 slpm, and the diluting nitrogen is supplied at approximately 20 slpm. The second gas mixture includes steam, which is created by the reaction of hydrogen and oxygen, as well as nitrogen, and any unreacted precursor gases. This operational phase is referred to as a wet oxidation. The wet oxidation takes place for approximately 6 minutes. The second gas mixture is transferred to the furnace via plumbing, such as for example stainless steel tubing. In one embodiment of the present invention the second gas mixture is maintained at 180° C. as it passes through the stainless steel tubing on its way to the showerhead of the furnace. No significant amount of H2 exits the catalytic reaction chamber.

[0034] Although the furnace is maintained at approximately 625° C. in the illustrative embodiment of the present invention, it is possible to maintain a temperature gradient through the furnace such that, for example, one end of the furnace is cooler and the other end is hotter. As is well-known in this field, modern furnace controllers provide users with the ability to program such temperature gradients, specifying times and temperatures.

[0035] Subsequent to the wet oxidation, the wafers are annealed in N2 for approximately 30 minutes. Then the wafers are pulled out of the furnace. In this illustrative embodiment, the time taken for loading the wafers, pushing them into the furnace, completing the dry and wet oxidation operations, annealing, pulling the wafers out of the furnace and unloading is approximately 3.5 hours.

[0036] A second exemplary process for the formation of an oxide of silicon suitable for use as a MOSFET gate dielectric is described in conjunction with FIG. 3, and includes forming a gate electrode and source/drain terminals needed to complete a MOSFET. It will be appreciated that apparatus and methods in accordance with the present invention can produce gate dielectric layers suitable for both PFETs and NFETs.

[0037] Referring to FIG. 3, oxygen and nitrogen are provided to a vertically oriented furnace and wafers are pushed into the furnace at a rate of approximately 500 mm per minute (block 302) as the temperature is maintained at approximately 500° C. The furnace temperature is then ramped from approximately 500° C. to approximately 625° C. (304). The wafers are typically in a container and the container is pushed into the furnace by a mechanism which is also adapted to rotate the wafers by rotating the container. A container of approximately 125 eight-inch wafers is rotated at approximately 3 rpm. After the wafers are in the furnace, a dry oxidation operation is performed (block 306) in which a first gas mixture including HCl, CO2, N2, and O2 is provided to the furnace, and a temperature of approximately 625° C. is maintained. The HCl and CO2 are produced external to the furnace in a reaction chamber in which dichloroethylene and oxygen react at approximately 800° C. After approximately 2 minutes, the flow of the first gas mixture is stopped and a second gas mixture is provided to the furnace (block 308). The second gas mixture includes catalytically produced steam along with molecular nitrogen. The steam is maintained at approximately 180° C. as it is piped from the external catalytic reaction chamber to the furnace. After approximately 6 minutes, the flow of the second gas mixture is stopped and the wafers are subjected to a 30 minute anneal in a nitrogen ambient (block 310). Subsequently, the wafers are removed from the furnace (block 312).

[0038] Still referring to FIG. 3, after the oxide dielectric layer has been formed, conventional processing operations may be performed in order to form a gate electrode over the dielectric layer, and to form source/drain terminals substantially aligned with the gate electrode (block 314). For example, a layer of polysilicon may be formed of the oxide, patterned with a gate mask, to form one or more gate electrodes. Source/drain terminal formation can be accomplished by any of a number of well-known methods. For example, a first ion implantation, aligned to the gate electrode to form a source/drain extension can be performed, followed by formation of sidewall spacers along laterally opposed sides of a gate electrode, and followed in turn by a second ion implantation to form the deep portions of the source/drain terminals. Those skilled in the art will recognize that both NFETs and PFETs can be formed in this way. The type of dopant ions implanted depends of the type of transistor being formed. For example, PFETs have p-type source/drains which can be formed by dopants such as boron or indium. Similarly, NFETs have n-type source/drains which can be formed by dopants such as phosphorus, arsenic or antimony.

[0039] Various other layers of insulators and conducting material are formed above the gate level, as is well understood in the field of semiconductor manufacturing and integrated circuit design.

CONCLUSION

[0040] Embodiments of the present invention provide extremely thin dielectric layers. Dielectric layers less than or equal to approximately 11 angstroms, which are suitable for use as the gate insulating layer for FETs, are created in a dry/catalytic steam oxidation process which provides a uniformity 0.5 angstrom at 3&sgr;.

[0041] It will be recognized by those skilled in the art and having the benefit of this disclosure that the present invention is applicable to the formation of both n-channel FETs (NFETs) and p-channel FETs (PFETs).

[0042] The present invention may be implemented with various changes and substitutions to the illustrated embodiments. For example, the present invention may be practiced with not only with silicon wafers as substrates, but also with other substrates, including but not limited to such substrates as silicon on insulator (SOI) Various other carrier and diluting gases may be substituted for nitrogen and provide substantially similarly results, however, nitrogen is typically preferred because it is much less expensive than other substantially inert gases. Furthermore, those skilled in the art and having the benefit of the present disclosure will recognize that times, temperatures, and rotational speeds may need to be varied to accommodate different size wafers (e.g., 300 mm diameter wafers) or different numbers of wafers in the furnace. Variation of these parameters in view of the present disclosure would be an undertaking which does not require undue experimentation by those skilled in the art.

[0043] Although specific embodiments, including specific equipment, parameters, methods and materials have been described, it will be readily understood by those skilled in the art and having the benefit of this disclosure, that various other changes in the details, materials, and arrangements of the materials and steps which have been described and illustrated in order to explain the nature of this invention may be made without departing from the principles and scope of the invention as expressed in the subjoined claims.

Claims

1. An apparatus, comprising:

a furnace having an opening at one end to receive a wafer container, and having a showerhead gas receiver at a second end;

a first reaction chamber adapted to receive 1,2-dichloroethylene and oxygen, and having a first output port;

a second reaction chamber adapted to receive O2, H2, and N2, the second reaction chamber having a catalyst therein, and a second output port; and

a source of diluting gas;

wherein the source of diluting gas and the first output are coupled to the showerhead through a first pathway, and the second output port is coupled to the showerhead through a second pathway.

2. The apparatus of claim 1, further comprising a bubbler containing liquid 1,2-dichloroethylene coupled to the first reaction chamber.

3. The apparatus of claim 1, further comprising a push mechanism, coupled to the furnace, adapted to provide rotational velocity to the wafer container.

4. The apparatus of claim 1, wherein the second pathway comprises stainless steel tubing fitted with a thermal jacket for maintaining a desired temperature.

5. The apparatus of claim 1, wherein the catalyst comprises a material that promotes the formation of steam from O2 and H2 without flaming.

6. The apparatus of claim 1, wherein the diluting gas comprises N2.

7. The apparatus of claim 1, further comprising an H2 detector coupled to the second output port.

8. A method of forming a dielectric layer on a surface of a substrate, comprising:

maintaining at least one substrate in a furnace at a temperature of approximately 625° C.;

rotating the at least one substrate;

providing diluted HCl, CO2, and O2 to a first end of the furnace; and

providing diluted steam the first end of the furnace.

9. The method of claim 8, wherein diluted HCl, CO2, and O2 is diluted with N2.

10. The method of claim 8, wherein diluted steam is diluted with N2.

11. The method of claim 8, further comprising reacting 1,2-dichloroethylene and oxygen to produce at least HCl and CO2.

12. The method of claim 8, further comprising catalytically reacting O2 and H2 in the presence of N2 at a temperature of approximately 500° C.

13. The method of claim 8, wherein the at least one substrate comprises a silicon wafer.

14. The method of claim 8, wherein rotating the at least one substrate comprises rotating at approximately 3 rpm.

15. The method of claim 8, wherein the at least one substrate comprises at least 100 silicon wafers each having a diameter of substantially 200 mm; and wherein the wafers are rotated at approximately 3 rpm.

16. The method of claim 8, wherein diluted HCl, CO2, and O2 are provided to the furnace at atmospheric pressure.

17. The method of claim 8, wherein providing diluted HCl, CO2, and O2 is substantially stopped prior to providing diluted.

18. The method of claim 8, wherein the dielectric layer is an oxide of silicon having a 3&sgr; uniformity of 0.5 angstroms.

19. The method of claim 8, wherein the furnace is vertically oriented and the first end is the top end.

20. A method of making a field effect transistor, comprising:

providing oxygen and nitrogen to a furnace;

pushing one or more wafers into the furnace;

rotating the one or more wafers at approximately 3 rpm

providing HCl, CO2, N2, and O2 to the furnace and maintaining a temperature of approximately 625° C.;

providing N2 and steam, at approximately 180° C., to the furnace;

removing the one or more wafers from the furnace;

patterning at least one gate electrode on the one or more wafers; and

forming source/drain terminals substantially adjacent the gate electrode.

21. The method of claim 20, further comprising nitridizing an oxide layer on a surface of the wafer prior to patterning at least one gate electrode on the wafer.

22. The method of claim 20, wherein providing HCl, CO2, N2, and O2 continues for approximately 2 minutes.

23. The method of claim 20, wherein providing steam and N2, continues for approximately 6 minutes.

24. The method of claim 20, further comprising annealing the one or more wafers.

25. The method of claim 24, wherein annealing comprises maintaining the one or more wafers at approximately 625° C., in a nitrogen ambient for approximately 30 minutes.

26. An oxide furnace system, comprising

a furnace having a gas inlet at a first end, and a wafer receiving port at a second end;

a dry chlorinated oxygen generator coupled to the gas inlet;

a catalytic steam generator coupled to the gas inlet;

a push mechanism, aligned with the wafer receiving port, adapted to provide linear and rotational velocity to a plurality of wafers; and

a temperature-controlled pathway disposed between the catalytic steam generator and the gas inlet;

wherein the dry chlorinated oxygen generator and the catalytic steam generator are spaced apart from the furnace and coupled to the gas inlet of the furnace by plumbing.

27. The oxide furnace of claim 26, further comprising a furnace controller coupled to the furnace.

28. The oxide furnace of the claim 26, further comprising an H2 detector coupled to the output of the catalytic steam generator.

29. The oxide furnace of claim 26, further comprising an alarm coupled to the H2 detector.