rdlc data matrix

rdlc data matrix

rdlc data matrix

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As shown in Figure 6.31, use the Show Related Records From menu near the top of the Portal Setup dialog to choose the OrderLines table from the group of related tables appearing in the list. Then select the Allow Deletion of Portal Records checkbox and enter 8 into the Number of Rows field. Also, select the Alternate Background Fill checkbox and choose the second lightest gray from the adjacent color palette. When you re finished, click OK to accept the portal setup. Immediately upon dismissing the Portal Setup dialog, you see the Add Fields to Portal dialog. In the column at the left, select the OrderLines::Qty field and click the button labeled Move to include it in the column at the right of the dialog. Repeat this procedure to include the OrderLines::ItemID field, the OrderLines::Price field, and the OrderLines:: cLineTotal field (as shown in Figure 6.32). When complete, click the OK button. You now have a portal on the Orders layout, but it needs some further configuration before it s ready for use. To complete the process, proceed as follows:

You may have noticed that some FSCommands have already been entered on other keyframes of the countdown.fla movie. These have been placed to ensure that the background color stays consistent with other settings, regardless of where playback occurs.

or x-ray), the energy of the radiation, and the density of the absorber. By comparing the amount of exposure of lm behind each strip (including a fourth uncovered area), some estimate as to the type and energy of the radiation can be determined. Unlike the pen dosimeter, which can be read by the user, the lm badge must be sent to an outside laboratory for interpretation.

at 450-725 C and above 70 atm, it gave a higher yield of light products The accumulation of coke, which required cessation of operation, was eliminated by what was described as "the clean circulation principle" When the Dubbs process was first demonstrated, refiners were astounded by the fact that the plant operated continuously for 10 days, establishing a world record for length of operation, quantity of oil processed, and yield of gasoline produced Excessive coke formation nevertheless is a serious shortcoming of thermal cracking processes Since high olefin yields are characteristic of thermal cracking, the process still plays an important role in olefin manufacture The temperature range 425-525 C and pressures of ",25-70 atm are used The thermal cracking process, however, could not meet the high demand for quality gasoline.

During World War I a new industrial process, catalytic cracking, was introduced for the production of gasoline from petroleum based on the Lewis acid aluminum chloride 4 A nonaromatic oil was slowly distilled from 3-5% AICl 3 at atmospheric pressure until the liquid temperature reached 225 C The distilled product had a high octane number and a low sulfur content when compared to thermally cracked products This process was later replaced by treatment of residual oils with acidic clays5-8 Known as the Houdry process, it used acid-treated montmorillonite at 450 C yielding gasoline of even higher octane number 8- 10 The clay was rapidly deactivated by the formation of coke but could be regenerated by burning off the carbon with hot air Natural clay catalysts were replaced by amorphous synthetic silica-alumina catalysts5,11 prepared by coprecipitation of orthosilicic acid and aluminum hydroxide.

104 Table 3.3. Rel 97/98 QoS attribute Precedence class Delay class Reliability class Throughput class

After calcining, the final active catalyst contained 10-15% alumina and 8590% silica Alumina content was later increased to 25% Active catalysts are obtained only from the partially dehydrated mixtures of the hydroxides Silicamagnesia was applied in industry, too Since the early 1960s, the synthetic amorphous silica-alumina catalysts have been to a large extent replaced by catalysts containing up to 15% zeolites and crystalline aluminosilicates in an amorphous matrix 12- 19 The first catalysts were synthetic faujasites (Linde X) modified with rare-earth metal ions by ion exchange These active catalysts give up to 10-50% higher yields of gasoline than the completely amorphous catalysts, with high selectivity and lowered coking A rare-earth form of zeolite Y (REHY) with improved chemical and hydrothermal stability was introduced later 14-16 Ultrastable hydrogen-exchanged zeolite (USY) and the use of medium-pore ZSM-5 are significant developments.

FIGURE 18.5 An illustration placed on a page in portrait orientation (upper left), landscape orientation (lower left), portrait with Transverse selected (upper right), and landscape with Transverse selected (lower right)