Page 352 - Sami Franssila Introduction to Microfabrication
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Tools for CVD and Epitaxy 331



               Table 33.1 LPCVD of silicon nitride (Si 3 N 4 )  constant and gas introduction is made uniform by an
                                                       elaborate distribution system. Alternatively ‘poly’ can
           If wafers come directly from another furnace operation  be deposited in amorphous state at 570 C to eliminate
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            (e.g., LOCOS pad oxide growth), no cleaning is  grain size gradients.
            required. Time limit for a new clean can be set, for
            example, at 2 h.
           Load the wafers in the boat, fill with dummy wafers to  33.3 ALD (ATOMIC LAYER DEPOSITION)
            equalize load and flow patterns.
                                    ◦
           Ramp temperature from 500 to 750 C under nitrogen  Surface-controlled reactions result in better step cover-
            flow, 50 min (5 C/min).                     age (microscale phenomenon) and uniformity across the
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           Pump to vacuum and perform leak check, 2 min.  wafer (macroscale phenomenon) compared to transport-
           Introduce ammonia NH 3 , stabilize flow at 30 sccm, for  limited reactions. ALD (which is also known as atomic
            1 min.                                     layer CVD) is the ultimate surface-reaction limited case:
           Introduce dichlorosilane SiH 2 Cl 2 , flow 120 sccm,  one atomic layer is deposited in a single pulse of reac-
            deposition starts.                         tant gases. The first layer to react at the surface (AB)
           Deposit at 300 mtorr for 25 min (thickness 100 nm, or  is chemisorbed with bond energies of the order of 1 eV,
            4 nm/min deposition rate).                 while additional layers are physisorbed with bond ener-
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           Cool down to 700 C (10 min).                gies of the order of 0.4 eV. By selecting temperature
           Boat out.                                   and flush-gas pulses suitably, it can be arranged so that
           Measurement: film thickness and refractive index  chemisorbed species are stable and physisorbed species
            monitoring by the ellipsometer.
                                                       and the excess precursor are flushed away. With the
                                                       desorption time for the chemisorbed species at least of
                                                       the order of seconds and residence time for physisorbed
           LPCVD (Figure 33.2) and oxidation tubes can be fitted  species a fraction of second, only the chemisorbed layer
           to the same furnace stack. A process for LPCVD silicon  will remain. A second pulse of a different precursor
           nitride (Table 33.1) bears similarity to oxidation process  (CD) is then introduced and allowed to react with the
           (Table 31.1).                               adsorbed species AB to form solid film according to
             Flow, temperature and pressure are important CVD
           reactor design criteria. Practically all CVD processes  AB (adsorbed) + CD (adsorbed) −→
           use toxic, corrosive and flammable fluids such as              AD (solid) + BC (gas)  (33.7)
           ammonia, silane, dichlorosilane, hydrides and metal
           organics. Reactor designs include double piping, inert  ZrCl 4 (ad) + 2H 2 O (ad) −→
           gas flushing and venting and other safety features. Some       ZrO 2 (s) + 4HCl (g)  (33.8)
           of the reaction byproducts are harmful to pumps and
           mechanical constructions, which translates to special  Repeated cycles of pulses of precursors AB and CD
           care in materials selection. Environmental, safety and  lead to the growth of solid film AD. Layer thickness is
           health issues will be discussed further in Chapter 35.  given by the number of pulses multiplied by monolayer
             CVD furnace systems are hot-wall systems, meaning  thickness. In theory, one monolayer per pulse is
           that deposition also takes place on the walls. This leads  deposited, but in many cases a sub-monolayer growth
           to film build-up and flaking problems.        is seen.
             Gases are introduced in one end of the tube.  In both cases, however, growth is self-limiting.
           Deposition leads to reactant gas depletion towards  Practical growth rates range around 1 ˚ A/cycle: for Al 2 O 3
           the end of the tube, and boundary-layer thickness  deposition, it is 1.1 ˚ A/cycle and for TiN, it is 0.2 ˚ A/cycle
           increase also reduces deposition rate. However, this is  (for other precursor gases this can, of course, be very
           compensated by increased temperature (=increased rate  different). When thickness/cycle numbers are translated
           of chemical reaction). Heating elements are arranged in  into deposition rates, one has to take into account the
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           three zones: for example, T1: 747 C, T2: 750 C and  flushing cycles between the pulses. Overall rates of a
           T3: 753 C for LPCVD silicon nitride (Figure 33.2).  few nanometres per minute are typical for ALD, similar
                 ◦
           This temperature ramp along the tube helps to keep  to LPCVD nitride or polysilicon, which are much higher
           deposition rate constant.                   temperature processes. ALD is a slow process, but there
             In polysilicon LPCVD, this three-zone system results  are many applications in which very thin films are
           in grain size gradient along the length of the tube.  needed, and step coverage requirements are strict: for
           In so-called flat-poly systems, the temperature is kept  example, diffusion barrier deposition into a high aspect
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