
4.2Piping ST 3000 Transmitter, Continued
Piping Arrangements, |
| Another piping arrangement uses a | ||||||||||||||||||||||
continued |
| the process piping to the transmitter as shown in Figure 12. | ||||||||||||||||||||||
| Figure 12 | Typical Arrangement for ½” NPT Process Connection Piping | ||||||||||||||||||||||
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| Tank Wall | |||||||||||||||||||||
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| 1/2" NPT | ||||||||||||||||||
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| Connection | ||||||||||||||||||
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Transmitter location |
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| Table 11 lists the mounting location for the transmitter depending on | ||||||
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| Table 11 | Suggested Transmitter Location for Given Process | ||||||
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| Process | Suggested Location | Explanation |
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| Gases | Above the gas line | The condensate drains away from |
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| the transmitter. |
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| Liquids | 1. Below but close to the | 1. This minimizes the static head |
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| elevation of the process | effect of the condensate. |
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| connection. |
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| 2. Level with or above the | 2. This requires a siphon to |
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| process connection. | protect the transmitter from |
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| process steam. The siphon |
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| retains water as a “fill fluid.” |
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| For liquid or steam, the piping should slope a minimum of 25.4 mm | ||||
| ATTENTION |
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| (1 inch) per 305 mm (1 foot). Slope the piping down towards the | ||||
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| transmitter if the transmitter is below the process connection so the | ||||
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| bubbles may rise back into the piping through the liquid. If the | ||||
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| transmitter is located above the process connection, the piping should | ||||
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| rise vertically above the transmitter; then slope down towards the | ||||
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| flowline with a vent valve at the high point. For gas measurement, use a | ||||
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| condensate leg and drain at the low point (freeze protection may be | ||||
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| required here). |
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| Continued on next page | ||
2/05 | ST 3000 Release 300 Installation Guide | 35 |