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                        TELEDYNE  
HASTINGS 
INSTRUMENTS 
INSTRUCTION MANUAL 
HFM-300 FLOW METER, 
HFC-302 FLOW CONTROLLER 
ISO 9001
CER T IFIED                                                                                                                                                                                                                                                                                                                                                                                            
                    
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                        Manual Print History  The print history shown below lists the printing dates of all revisions and addenda created for this  manual. The revision level letter increases alphabetically as the manual undergoes subsequent  updates. Addenda, which are released between revisions, contain important change information that  the user should incorporate immediately into the manual. Addenda are numbered sequentially. When a  new revision is created, all addenda associated with the previous revision of the 
                    
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                        Table of Contents    1. GENERAL INFORMATION............................................................................................................................................ 4  1.1. FEATURES.................................................................................................................................................................... 4  1.2. SPECIFICATIONS.................................................................................................................
                    
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                        1.  General Information      The Teledyne Hastings HFM-300 is used to measure mass flow rates in gases.  In addition to flow rate  measurement, the HFC-302 includes a proportional valve to accurately control gas flow. The Hastings mass flow  meter (HFM-300) and controller (HFC-302), hereafter referred to as the Hastings 300 series, are intrinsically  linear and are designed to accurately measure and control mass flow over the range of 0-5 sccm to 0-10 slm   with an accuracy of better than  ±0.75
                    
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                        1.2. Specifications  Accuracy .................................................................................... < ±0.75% full scale (F.S.) at 3σ  (±1.0% F.S. for >10 slm versions)  Repeatability .............................................................................±0.05% of reading + 0.02% F.S.  Maximum Pressure........................................................................................500 psi [3.45 MPa]  (With high pressure option) 1000 psi [6.9 MPa]  Pressure Coefficient 
                    
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                        The 4-20 mA I/O option can accept a current input.  The 0-5 VDC command signal on pin 14 can be  replaced by a 4-20mA command signal.  The loop presets an impedance of 75 ohms and is returned to  the power supply through the valve common.                                      1.4. Other Accessories  1.4.1. Hastings Power supplies  Hastings Power Pod power supply/display units are available in one and four channel versions. They  convert 100, 115 or 230VAC to the ±15 VDC required to operate the fl
                    
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                        2. Installation and Operation    This section contains the steps necessary to assist in getting a new flow meter/controller into  operation as quickly and easily as possible.  Please read the following thoroughly before attempting to  install the instrument.  2.1. Receiving Inspection  Carefully unpack the Hastings unit and any accessories that have also been ordered.  Inspect for any  obvious signs of damage to the shipment.  Immediately advise the carrier who delivered the shipment  if any dam
                    
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                        2.4. Mechanical Connections  2.4.1. Filtering  The smallest of the internal passageways in the Hastings 300 is the diameter of the sensor tube, which  is 0.026”(0.66 mm), and the annular clearance for the 500 sccm shunt which is 0.006"(0.15 mm) (all  other flow ranges have larger passages), so the instrument requires adequate filtering of the gas supply  to prevent blockage or clogging of the tube.   2.4.2. Mounting  There are two mounting holes (#8-32 thread) in the bottom of the transducer tha
                    
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                                              Fig. 2.1 Fig. 2.2       Figures 2.1/2.2, and Tables 2.1/2.2, show the 300/302 pin out.  Table 2.1 Table 2.2 "U" Pin-Out "H" Pin-Out Pin # Pin # 1 Signal Common 1 Do not use 2 Do not use 2 Do not use 3 Do not use 3 Do not use 4 +15 VDC 4 Do not use 5 5 Signal Common 6 Output 0-5 VDC (4-20mA) 6 Output 0-5 VDC (4-20mA) 7 Signal Common 7 Case Ground 8 Case Ground 8 Valve Override 9 Valve Override 9 -15VDC 10 10 Do not use 11 -15VDC 11 +15VDC 12 External Input 12 Signal Common 1
                    
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                        2.6.2. Zero Check  Turn the power supply on if not already energized.  Allow for a 1 hour  warm-up.  Stop all flow through the instrument and wait 2 minutes.   Caution:  Do not assume that all metering valves completely shut off  the flow.  Even a slight leakage will cause an indication on the meter  and an apparent zero shift.  For the standard 0-5 VDC output, adjust  the zero potentiometer located on the inlet side of the flow meter  until the meter indicates zero (Fig 2.3).  For the optional 
                    
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                        Span Error Vs. Pressure Fig. 2.5  0.017" Sensor 5% 4% 3% 2% 1% 0% Mean Max -1% Min -2% 0 100 200 300 400 500 600 700 800 900 1000 Pressure (psig)     If the system pressure is higher than 250 psig (1.7 MPa) the pressure induced error in the span reading  becomes significant.  The charts above show the mean error enveloped by the minimum/maximum  expected span errors induced by high pressures.  This error will approach 16% at 1000 psig.  For  accurate high pressure measurements this error must be
                    
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                        The first method requires that the two controllers use the same signal range (0 to 5 VDC or 4 to 20 mA)  and that they be sized and calibrated to provide the correct ratio of gasses. Then, by routing the  actual flow Output signal from the primary meter/controller through the secondary controller’s  External Input pin (See Tables 2.1 & 2.2), the ratio of flows can be maintained over the entire range of  gas flows.  EXAMPLE:  Flow controller A has 0-100 slpm range with a 5.00 volt output at full 
                    
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                        variable directly.  This analog output signal could be 0-5 volts, 0-10 volts (or 4-20 ma for units with 4- 20 ma boards) or any value in between.  On the controller card there is a jumper that sets whether the control loop controls mass flow or an  external process variable.  See Figure 2.7.  If the jumper is over the top two pins, the loop controls  mass flow.  If the jumper is over the bottom two pins, the loop controls an external process variable.   This process variable signal must be suppl
                    
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                        2.12. Temperature Coefficients  As the ambient temperature of  Fig. 2.8  the instrument changes from  the original calibration  temperature, errors will be  introduced into the output of  the instrument.  The  Temperature Coefficient of  Zero describes the change in  the output that is seen at zero  flow.  This error is added to the  overall output signal regardless  of flow, but can be eliminated  by merely adjusting the zero  potentiometer of the flow  meter/controller to read zero  volts at z
                    
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                        3. Theory of Operation    This section contains an overall functional description of the Hastings 300 series of flow instruments.   In this section and other sections throughout this manual, it is assumed that the customer is using a  Hastings power supply.     3.1. Overall Functional Description  The Hastings 300 meter consists of a sensor, base, and a shunt.  In addition to the components in a  meter, The 300 controller includes a control valve and extra electronic circuitry.  The sensor is  c
                    
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                        low temperatures used by the sensor, and because the sensor construction preferentially favors the  conductive and convective heat transfer modes.  The thermal energy of each heater will then be  dissipated by conduction down the stainless steel sensor tube, conduction to the insulating foam, plus  the convection due to the mass flow of the sensed gas.   Because great care is taken to wind the resistive heater coils symmetrically about the midpoint of the  tube, it is assumed that the heat condu
                    
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                        The gas stream will increase in temperature due to the heat it gains from the upstream heater. This  elevated gas stream temperature causes the heat transfer at the downstream heater to gain heat from  the gas stream. The heat gained from the gas stream forces the downstream bridge control loop to  apply less power to the downstream heater coil in order to maintain a constant differential  o temperature of 48 C.    The power difference at the RTD’s is a function of  the mass flow rate and the sp
                    
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                        the shunt.  Most instruments employ  Poiseuille’s law and use some sort of  multi-passage device that creates  laminar flow between the upstream  sensor inlet and the downstream outlet.   This makes the volumetric flow versus  pressure drop curve primarily linear, but  there are other effects which introduce  higher order terms.  Most flow transducers are designed such  that the outlet plenum has a smaller  diameter than the inlet plenum.   This  eases the insertion and containment of  the shunt
                    
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                        Qρ                           L =  (3.5)  e 5πμ For a typical flow divider tube the entry length is approximately 0.16 cm.  From this it can be seen  that if the sensor inlet pickup point is inside of the flow divider tube but downstream of the entrance  length and if the sensor outlet point is inside the flow divider tube but upstream of the exit point then  the pressure drop that drives the flow through the sensor would be linear with respect to volumetric  flow rate.  Since the pressure drop a
                    
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                        Fig. 3.5 Thickness of the annular ring as a function of flow rate     for a sensor with a 75 Pa drop and a 2 cm spacing.    0.18     0.16      0.14     0.12     0.1     0.08     0.06     0.04       0.02     0   0 5 10 15 20 25 30 35 Flow (liter/min)   Each shunt must have a section of the annular region upstream of the upstream sensor tap to allow the  flow to become fully developed before reaching the first tap.  The entry length for the annular passage  is then:     Qρ() Δr