Steam Flow Measurement - PowerPoint PPT Presentation

About This Presentation
Title:

Steam Flow Measurement

Description:

By- D K Singhal. Disclaimer ... will be indicated by a reduction in ... The line pressure can be measured by the pressure gauge mounted on the unit, as ... – PowerPoint PPT presentation

Number of Views:372
Avg rating:3.0/5.0
Slides: 15
Provided by: paper4
Category:
Tags: by | flow | measurement | steam

less

Transcript and Presenter's Notes

Title: Steam Flow Measurement


1
Steam Flow Measurement
  • By-
  • D K Singhal

2
Disclaimer
  • This presentation is supplied as a self learning
    presentation, and is subjected to the condition
    that the author accepts no liability from the use
    of the same or from the techniques or information
    provided within the same.
  • It is strongly recommended to consult your
    mechanical engineer, process engineer and other
    technical experts, before making any changes to
    the existing system.

3
Preface
  • Steam consumption is one of the significant cost
    factors in paper and other process industries. In
    absence of any steam flow metering control and
    optimization of steam consumption is not
    possible.

4
Available Systems
  • Steam flow measurement systems available in the
    market are very costly, and hence most of the
    mills cannot afford them to install. But, nothing
    can be controlled if it is not being monitored.

5
Proposed System
  • This must be indicated that the proposed system
    is of very low cost. In the proposed system,
    reading is taken from the instrument and with the
    help of calibration chart, steam flow is
    estimated. Accuracy may be a little lower, but
    benefits obtained by the proposed system may even
    encourage the user to purchase and install steam
    flow meter from a reputed supplier.

6
Concept
  • Pressure Drop across a saturated steam pipeline
    is a function of steam flow rate, steam pressure
    (and hence specific volume) and pipe diameter.
  • For most of the cases, steam pressure is normally
    kept constant, or varies within narrow limits.
    Pipe diameter, of course, is fixed for a
    particular position.

7
Steam Flow
  • The proposed system works on the basis of
    pressure drop in a horizontal steam pipeline,
    which is proportionate to square of steam flow
    rate. i.e. for any flow rate say pressure
    difference is 100mmWC, a 10 reduction in steam
    flow will be indicated by a reduction in pressure
    drop to 79mmWC. Thus, one can very easily achieve
    the optimum steam consumption for a particular
    application.

8
Schematic Drawing

  • Distance for which dP is to be
    measured

Steam Flow
Pressure Gauge
Gauge Glass Assly.
Closed Tank
Zero Level
Baffle Plate
Steam Trap
T
9
About the Equipment
  • As indicated in figure, the tank has a partition
    in the center. The lower chamber is filled with
    water upto zero level prior to installation. Any
    further water coming into the tank is drained
    from the excess water removal line through valve
    and steam trap installed, as indicated in the
    left side of figure.

10
Operation
  • Initially, the lower chamber is filled with
    water. When the system is connected to steam
    line, steam from upstream side fills lower
    chamber and exerts a pressure inside gauge glass.
    The downstream side steam pressure fills upper
    chamber and tries to counterbalance the upstream
    pressure. The pressure drop is indicated in the
    gauge glass.

11
Initial Measurements
  • Distance between the two points at which the unit
    is connected is measured. Steam pipe diameter is
    also measured. The line pressure can be measured
    by the pressure gauge mounted on the unit, as
    indicated in schematic.
  • Gauge glass initial level is marked when there is
    no steam flow. Any increase in gauge glass level,
    thus, can be measured.
  • Also, the pressure can be measured by the
    pressure gauge mounted on the unit.

12
Flow Estimation
  • The steam flow will be proportional to the square
    root of gauge glass level increase, and inversely
    proportional to the steam pressure as indicated
    by the pressure gauge.
  • Formulae are available to calculate pressure drop
    in the pipeline, and depending on the distance
    between two points in the steam line, working
    pressure, pipe diameter etc., it is possible to
    develop a plant specific correlation.

13
Flow Optimization
  • To optimize the steam flow, just measure gauge
    glass level increase at a particular operating
    condition and pressure.
  • After altering process variables, if the gauge
    glass reading decreases, it will clearly indicate
    that the steam flow has reduced.

14
Feedback
  • Please send in your comments on this presentation
    to-
  • D K Singhal
  • Deveshksinghal_at_rediffmail.com
  • Deveshksinghal_at_gmail.com
  • Thank You.
Write a Comment
User Comments (0)
About PowerShow.com