Chemical production operation record
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Production Log for the Chemical Production Workshop
Shift: 0:00–8:00 Shift: 8:00–16:00 Date: Year Month Day
Drum Cooling Section Desulfurization Section Crude Benzene Section Drum Cooling Section Desulfurization Section Crude Benzene Section
Suction pressure before machine (pa) Circulating fluid flow rate (m3/h) Gas temperature before final cooling tower (℃) Suction pressure before machine (pa) Circulating fluid flow rate (m3/h) Gas temperature before final cooling tower (℃)
Suction pressure before device (pa) Compressed air flow rate into regeneration tower (m3/h) Gas temperature after final cooling tower (℃) Suction pressure before device (pa) Compressed air flow rate into regeneration tower (m3/h) Gas temperature after final cooling tower (℃)
Gas temperature before device (℃) Sulfur production (t) Final cooling resistance (pa) Gas temperature before device (℃) Sulfur production (t) Final cooling resistance (pa) Collection temperature (℃)
Ammonium sulfate (ammonia evaporation) Gas temperature after benzene washing tower (℃) Collection temperature (℃) Ammonium sulfate (ammonia evaporation) Gas temperature after benzene washing tower (℃)
Pressure after machine (pa) Temperature after fractionator (℃) Temperature of lean oil entering the tower (℃) Pressure after machine (pa) Temperature after fractionator (℃) Temperature of lean oil entering the tower (℃)
Fan motor current (A) Tower top temperature (℃) Pressure after benzene washing tower (pa) Fan motor current (A) Tower top temperature (℃) Pressure after benzene washing tower (pa)
Cooling oil temperature (℃) Wastewater temperature (℃) Oil temperature at the exit of the tubular furnace (℃) Cooling oil temperature (℃) Wastewater temperature (℃) Oil temperature at the exit of the tubular furnace (℃)
Oil pressure (MPa) Amount of alkali added during ammonia evaporation Furnace temperature of the tubular furnace (℃) Oil pressure (MPa)
Ammonium sulfate section Furnace temperature of the tubular furnace (℃) Temperature of circulating ammonia water (℃) Ammonium sulfate section Temperature at the top of the benzene removal tower (℃) Temperature of circulating ammonia water (℃)
Resistance of the saturator (pa) Temperature at the top of the benzene removal tower (℃) Current of the circulation pump motor (A) Resistance of the saturator (pa) Steam pressure of the benzene removal tower (pa) Current of the circulation pump motor (A)
Preheater temperature (℃) Steam pressure of the benzene removal tower (pa) Temperature of the insulation box (℃) Preheater temperature (℃) Superheated steam temperature (℃) Temperature of the insulation box (℃)
Acidity of the mother liquor (%) Superheated steam temperature (℃) Voltage of the electrostatic precipitator (V) Acidity of the mother liquor (%) Total steam pressure (MPa) Voltage of the electrostatic precipitator (V)
Ammonium sulfate production (bags) Total steam pressure (MPa) Volume of gas fed for recovery Ammonium sulfate production (bags) Oil consumption for washing Volume of gas fed for recovery Ammonium sulfate production (bags) Oil consumption for washing
Volume of tar sent to the oil storage tank (t) Sulfuric acid consumption Volume of crude benzene sent to the oil storage tank Volume of tar sent to the oil storage tank (t) Sulfuric acid consumption Volume of crude benzene sent to the oil storage tank
Operational notes Shift supervisor:
Operational notes Shift supervisor:
Shift: 16:00–0:00 Drum Cooling Section Desulfurization Section Ammonium sulfate (ammonia evaporation) Crude Benzene Section Crude Benzene Section
Suction pressure before machine (pa) Oil pressure (MPa) Circulating fluid flow rate (m3/h) Amount of alkali added during ammonia evaporation Gas temperature before final cooling tower (℃) Furnace temperature of the tubular furnace (℃)
Suction pressure before device (pa) Temperature of circulating ammonia water (℃) Compressed air flow rate into regeneration tower (m3/h) Ammonium sulfate section Gas temperature after final cooling tower (℃)
Temperature at the top of the benzene removal tower (℃) Gas temperature before device (℃) Current of the circulation pump motor (A) Sulfur production (t) Resistance of the saturator (pa) Final cooling resistance (pa)
Steam pressure of the benzene removal tower (pa) Collection temperature (℃) Temperature of the insulation box (℃) Ammonium sulfate (ammonia evaporation) Preheater temperature (℃)
Gas temperature after benzene washing tower (℃) Superheated steam temperature (℃) Pressure after machine (pa) Voltage of the electrostatic precipitator (V) Temperature after fractionator (℃)
Acidity of the mother liquor (%) Temperature of lean oil entering the tower (℃) Total steam pressure (MPa) Fan motor current (A) Volume of gas fed for recovery
Tower top temperature (℃) Ammonium sulfate production (bags) Pressure after benzene washing tower (pa) Oil consumption for washing Cooling oil temperature (℃)
Volume of tar sent to the oil storage tank (t) Wastewater temperature (℃) Sulfuric acid consumption Oil temperature at the exit of the tubular furnace (℃) Volume of crude benzene sent to the oil storage tank
Operational notes Shift supervisor:
Shift: 0:00–8:00 Shift: 8:00–16:00 Date: Year Month Day
Drum Cooling Section Desulfurization Section Crude Benzene Section Drum Cooling Section Desulfurization Section Crude Benzene Section
Suction pressure before machine (pa) Circulating fluid flow rate (m3/h) Gas temperature before final cooling tower (℃) Suction pressure before machine (pa) Circulating fluid flow rate (m3/h) Gas temperature before final cooling tower (℃)
Suction pressure before device (pa) Compressed air flow rate into regeneration tower (m3/h) Gas temperature after final cooling tower (℃) Suction pressure before device (pa) Compressed air flow rate into regeneration tower (m3/h) Gas temperature after final cooling tower (℃)
Gas temperature before device (℃) Sulfur production (t) Final cooling resistance (pa) Gas temperature before device (℃) Sulfur production (t) Final cooling resistance (pa) Collection temperature (℃)
Ammonium sulfate (ammonia evaporation) Gas temperature after benzene washing tower (℃) Collection temperature (℃) Ammonium sulfate (ammonia evaporation) Gas temperature after benzene washing tower (℃)
Pressure after machine (pa) Temperature after fractionator (℃) Temperature of lean oil entering the tower (℃) Pressure after machine (pa) Temperature after fractionator (℃) Temperature of lean oil entering the tower (℃)
Fan motor current (A) Tower top temperature (℃) Pressure after benzene washing tower (pa) Fan motor current (A) Tower top temperature (℃) Pressure after benzene washing tower (pa)
Cooling oil temperature (℃) Wastewater temperature (℃) Oil temperature at the exit of the tubular furnace (℃) Cooling oil temperature (℃) Wastewater temperature (℃) Oil temperature at the exit of the tubular furnace (℃)
Oil pressure (MPa) Amount of alkali added during ammonia evaporation Furnace temperature of the tubular furnace (℃) Oil pressure (MPa)
Ammonium sulfate section Furnace temperature of the tubular furnace (℃) Temperature of circulating ammonia water (℃) Ammonium sulfate section Temperature at the top of the benzene removal tower (℃) Temperature of circulating ammonia water (℃)
Resistance of the saturator (pa) Temperature at the top of the benzene removal tower (℃) Current of the circulation pump motor (A) Resistance of the saturator (pa) Steam pressure of the benzene removal tower (pa) Current of the circulation pump motor (A)
Preheater temperature (℃) Steam pressure of the benzene removal tower (pa) Temperature of the insulation box (℃) Preheater temperature (℃) Superheated steam temperature (℃) Temperature of the insulation box (℃)
Acidity of the mother liquor (%) Superheated steam temperature (℃) Voltage of the electrostatic precipitator (V) Acidity of the mother liquor (%) Total steam pressure (MPa) Voltage of the electrostatic precipitator (V)
Ammonium sulfate production (bags) Total steam pressure (MPa) Volume of gas fed for recovery Ammonium sulfate production (bags) Oil consumption for washing Volume of gas fed for recovery Ammonium sulfate production (bags) Oil consumption for washing
Volume of tar sent to the oil storage tank (t) Sulfuric acid consumption Volume of crude benzene sent to the oil storage tank Volume of tar sent to the oil storage tank (t) Sulfuric acid consumption Volume of crude benzene sent to the oil storage tank
Operational notes Shift supervisor:
Operational notes Shift supervisor:
Shift: 16:00–0:00 Drum Cooling Section Desulfurization Section Ammonium sulfate (ammonia evaporation) Crude Benzene Section Crude Benzene Section
Suction pressure before machine (pa) Oil pressure (MPa) Circulating fluid flow rate (m3/h) Amount of alkali added during ammonia evaporation Gas temperature before final cooling tower (℃) Furnace temperature of the tubular furnace (℃)
Suction pressure before device (pa) Temperature of circulating ammonia water (℃) Compressed air flow rate into regeneration tower (m3/h) Ammonium sulfate section Gas temperature after final cooling tower (℃)
Temperature at the top of the benzene removal tower (℃) Gas temperature before device (℃) Current of the circulation pump motor (A) Sulfur production (t) Resistance of the saturator (pa) Final cooling resistance (pa)
Steam pressure of the benzene removal tower (pa) Collection temperature (℃) Temperature of the insulation box (℃) Ammonium sulfate (ammonia evaporation) Preheater temperature (℃)
Gas temperature after benzene washing tower (℃) Superheated steam temperature (℃) Pressure after machine (pa) Voltage of the electrostatic precipitator (V) Temperature after fractionator (℃)
Acidity of the mother liquor (%) Temperature of lean oil entering the tower (℃) Total steam pressure (MPa) Fan motor current (A) Volume of gas fed for recovery
Tower top temperature (℃) Ammonium sulfate production (bags) Pressure after benzene washing tower (pa) Oil consumption for washing Cooling oil temperature (℃)
Volume of tar sent to the oil storage tank (t) Wastewater temperature (℃) Sulfuric acid consumption Oil temperature at the exit of the tubular furnace (℃) Volume of crude benzene sent to the oil storage tank
Operational notes Shift supervisor:
Production Log for the Chemical Production Workshop
Shift: 0:00–8:00 Shift: 8:00–16:00 Date: Year Month Day
Drum Cooling Section Desulfurization Section Crude Benzene Section Drum Cooling Section Desulfurization Section Crude Benzene Section
Suction pressure before machine (pa) Circulating fluid flow rate (m3/h) Gas temperature before final cooling tower (℃) Suction pressure before machine (pa) Circulating fluid flow rate (m3/h) Gas temperature before final cooling tower (℃)
Suction pressure before device (pa) Compressed air flow rate into regeneration tower (m3/h) Gas temperature after final cooling tower (℃) Suction pressure before device (pa) Compressed air flow rate into regeneration tower (m3/h) Gas temperature after final cooling tower (℃)
Gas temperature before device (℃) Sulfur production (t) Final cooling resistance (pa) Gas temperature before device (℃) Sulfur production (t) Final cooling resistance (pa) Collection temperature (℃)
Ammonium sulfate (ammonia evaporation) Gas temperature after benzene washing tower (℃) Collection temperature (℃) Ammonium sulfate (ammonia evaporation) Gas temperature after benzene washing tower (℃)
Pressure after machine (pa) Temperature after fractionator (℃) Temperature of lean oil entering the tower (℃) Pressure after machine (pa) Temperature after fractionator (℃) Temperature of lean oil entering the tower (℃)
Fan motor current (A) Tower top temperature (℃) Pressure after benzene washing tower (pa) Fan motor current (A) Tower top temperature (℃) Pressure after benzene washing tower (pa)
Cooling oil temperature (℃) Wastewater temperature (℃) Oil temperature at the exit of the tubular furnace (℃) Cooling oil temperature (℃) Wastewater temperature (℃) Oil temperature at the exit of the tubular furnace (℃)
Oil pressure (MPa) Amount of alkali added during ammonia evaporation Furnace temperature of the tubular furnace (℃) Oil pressure (MPa)
Ammonium sulfate section Furnace temperature of the tubular furnace (℃) Temperature of circulating ammonia water (℃) Ammonium sulfate section Temperature at the top of the benzene removal tower (℃) Temperature of circulating ammonia water (℃)
Resistance of the saturator (pa) Temperature at the top of the benzene removal tower (℃) Current of the circulation pump motor (A) Resistance of the saturator (pa) Steam pressure of the benzene removal tower (pa) Current of the circulation pump motor (A)
Preheater temperature (℃) Steam pressure of the benzene removal tower (pa) Temperature of the insulation box (℃) Preheater temperature (℃) Superheated steam temperature (℃) Temperature of the insulation box (℃)
Acidity of the mother liquor (%) Superheated steam temperature (℃) Voltage of the electrostatic precipitator (V) Acidity of the mother liquor (%) Total steam pressure (MPa) Voltage of the electrostatic precipitator (V)
Ammonium sulfate production (bags) Total steam pressure (MPa) Volume of gas fed for recovery Ammonium sulfate production (bags) Oil consumption for washing Volume of gas fed for recovery Ammonium sulfate production (bags) Oil consumption for washing
Volume of tar sent to the oil storage tank (t) Sulfuric acid consumption Volume of crude benzene sent to the oil storage tank Volume of tar sent to the oil storage tank (t) Sulfuric acid consumption Volume of crude benzene sent to the oil storage tank
Operational notes Shift supervisor:
Operational notes Shift supervisor:
Shift: 16:00–0:00 Drum Cooling Section Desulfurization Section Ammonium sulfate (ammonia evaporation) Crude Benzene Section Crude Benzene Section
Suction pressure before machine (pa) Oil pressure (MPa) Circulating fluid flow rate (m3/h) Amount of alkali added during ammonia evaporation Gas temperature before final cooling tower (℃) Furnace temperature of the tubular furnace (℃)
Suction pressure before device (pa) Temperature of circulating ammonia water (℃) Compressed air flow rate into regeneration tower (m3/h) Ammonium sulfate section Gas temperature after final cooling tower (℃)
Temperature at the top of the benzene removal tower (℃) Gas temperature before device (℃) Current of the circulation pump motor (A) Sulfur production (t) Resistance of the saturator (pa) Final cooling resistance (pa)
Steam pressure of the benzene removal tower (pa) Collection temperature (℃) Temperature of the insulation box (℃) Ammonium sulfate (ammonia evaporation) Preheater temperature (℃)
Gas temperature after benzene washing tower (℃) Superheated steam temperature (℃) Pressure after machine (pa) Voltage of the electrostatic precipitator (V) Temperature after fractionator (℃)
Acidity of the mother liquor (%) Temperature of lean oil entering the tower (℃) Total steam pressure (MPa) Fan motor current (A) Volume of gas fed for recovery
Tower top temperature (℃) Ammonium sulfate production (bags) Pressure after benzene washing tower (pa) Oil consumption for washing Cooling oil temperature (℃)
Volume of tar sent to the oil storage tank (t) Wastewater temperature (℃) Sulfuric acid consumption Oil temperature at the exit of the tubular furnace (℃) Volume of crude benzene sent to the oil storage tank
Operational notes Shift supervisor:
Shift: 0:00–8:00 Shift: 8:00–16:00 Date: Year Month Day
Drum Cooling Section Desulfurization Section Crude Benzene Section Drum Cooling Section Desulfurization Section Crude Benzene Section
Suction pressure before machine (pa) Circulating fluid flow rate (m3/h) Gas temperature before final cooling tower (℃) Suction pressure before machine (pa) Circulating fluid flow rate (m3/h) Gas temperature before final cooling tower (℃)
Suction pressure before device (pa) Compressed air flow rate into regeneration tower (m3/h) Gas temperature after final cooling tower (℃) Suction pressure before device (pa) Compressed air flow rate into regeneration tower (m3/h) Gas temperature after final cooling tower (℃)
Gas temperature before device (℃) Sulfur production (t) Final cooling resistance (pa) Gas temperature before device (℃) Sulfur production (t) Final cooling resistance (pa) Collection temperature (℃)
Ammonium sulfate (ammonia evaporation) Gas temperature after benzene washing tower (℃) Collection temperature (℃) Ammonium sulfate (ammonia evaporation) Gas temperature after benzene washing tower (℃)
Pressure after machine (pa) Temperature after fractionator (℃) Temperature of lean oil entering the tower (℃) Pressure after machine (pa) Temperature after fractionator (℃) Temperature of lean oil entering the tower (℃)
Fan motor current (A) Tower top temperature (℃) Pressure after benzene washing tower (pa) Fan motor current (A) Tower top temperature (℃) Pressure after benzene washing tower (pa)
Cooling oil temperature (℃) Wastewater temperature (℃) Oil temperature at the exit of the tubular furnace (℃) Cooling oil temperature (℃) Wastewater temperature (℃) Oil temperature at the exit of the tubular furnace (℃)
Oil pressure (MPa) Amount of alkali added during ammonia evaporation Furnace temperature of the tubular furnace (℃) Oil pressure (MPa)
Ammonium sulfate section Furnace temperature of the tubular furnace (℃) Temperature of circulating ammonia water (℃) Ammonium sulfate section Temperature at the top of the benzene removal tower (℃) Temperature of circulating ammonia water (℃)
Resistance of the saturator (pa) Temperature at the top of the benzene removal tower (℃) Current of the circulation pump motor (A) Resistance of the saturator (pa) Steam pressure of the benzene removal tower (pa) Current of the circulation pump motor (A)
Preheater temperature (℃) Steam pressure of the benzene removal tower (pa) Temperature of the insulation box (℃) Preheater temperature (℃) Superheated steam temperature (℃) Temperature of the insulation box (℃)
Acidity of the mother liquor (%) Superheated steam temperature (℃) Voltage of the electrostatic precipitator (V) Acidity of the mother liquor (%) Total steam pressure (MPa) Voltage of the electrostatic precipitator (V)
Ammonium sulfate production (bags) Total steam pressure (MPa) Volume of gas fed for recovery Ammonium sulfate production (bags) Oil consumption for washing Volume of gas fed for recovery Ammonium sulfate production (bags) Oil consumption for washing
Volume of tar sent to the oil storage tank (t) Sulfuric acid consumption Volume of crude benzene sent to the oil storage tank Volume of tar sent to the oil storage tank (t) Sulfuric acid consumption Volume of crude benzene sent to the oil storage tank
Operational notes Shift supervisor:
Operational notes Shift supervisor:
Shift: 16:00–0:00 Drum Cooling Section Desulfurization Section Ammonium sulfate (ammonia evaporation) Crude Benzene Section Crude Benzene Section
Suction pressure before machine (pa) Oil pressure (MPa) Circulating fluid flow rate (m3/h) Amount of alkali added during ammonia evaporation Gas temperature before final cooling tower (℃) Furnace temperature of the tubular furnace (℃)
Suction pressure before device (pa) Temperature of circulating ammonia water (℃) Compressed air flow rate into regeneration tower (m3/h) Ammonium sulfate section Gas temperature after final cooling tower (℃)
Temperature at the top of the benzene removal tower (℃) Gas temperature before device (℃) Current of the circulation pump motor (A) Sulfur production (t) Resistance of the saturator (pa) Final cooling resistance (pa)
Steam pressure of the benzene removal tower (pa) Collection temperature (℃) Temperature of the insulation box (℃) Ammonium sulfate (ammonia evaporation) Preheater temperature (℃)
Gas temperature after benzene washing tower (℃) Superheated steam temperature (℃) Pressure after machine (pa) Voltage of the electrostatic precipitator (V) Temperature after fractionator (℃)
Acidity of the mother liquor (%) Temperature of lean oil entering the tower (℃) Total steam pressure (MPa) Fan motor current (A) Volume of gas fed for recovery
Tower top temperature (℃) Ammonium sulfate production (bags) Pressure after benzene washing tower (pa) Oil consumption for washing Cooling oil temperature (℃)
Volume of tar sent to the oil storage tank (t) Wastewater temperature (℃) Sulfuric acid consumption Oil temperature at the exit of the tubular furnace (℃) Volume of crude benzene sent to the oil storage tank
Operational notes Shift supervisor:
Production Log for Chemical Production Workshop Shift: 0:00-8:00 Shift: 8:00-16:00 Date: Year Month Day Drum Cooling Section Desulfurization Section Crude Benzene Section Drum Cooling Section Desulfurization Section Crude Benzene Section Absorption Pressure Before Machine (pa) Circulating Liquid Flow Rate (m3/h) Gas Temperature Before Final Cooling Tower (℃) Absorption Pressure Before Machine (pa) Circulating Liquid Flow Rate (m3/h) Gas Temperature Before Final Cooling Tower (℃) Absorption Pressure Before Unit Compressed Air Flow Rate into Regeneration Tower (m3/h) Gas Temperature After Final Cooling Tower (℃) Absorption Pressure Before Unit Compressed Air Flow Rate into Regeneration Tower (m3/h) Gas Temperature After Final Cooling Tower (℃) Gas Temperature Before Unit (℃) Sulfur Production (t) Final Cooling Resistance (pa) Gas Temperature Before Unit (℃) Sulfur Production (t) Final Cooling Resistance (pa) Collection Temperature (℃) Ammonium Sulfate (Ammonia Evaporation) Gas Temperature after Benzene Washing Tower (℃) Collection Temperature (℃) Ammonium Sulfate (Ammonia Evaporation) Gas Temperature after Benzene Washing Tower (℃) Pressure After Machine (pa) Temperature after Fractionator (℃) Temperature of Lean Oil Going into Tower (℃) Pressure After Machine (pa) Temperature after Fractionator (℃) Temperature of Lean Oil Going into Tower (℃) Fan Motor Current (A) Top Temperature of Tower (℃) Pressure after Benzene Washing Tower (pa) Fan Motor Current (A) Top Temperature of Tower (℃) Pressure after Benzene Washing Tower (pa) Coolant Oil Temperature (℃) Wastewater Temperature (℃) Oil Temperature at Exit of Tubular Furnace (℃) Coolant Oil Temperature (℃) Wastewater Temperature (℃) Oil Temperature at Exit of Tubular Furnace (℃) Oil Pressure (MPa) Amount of Alkali Added during Ammonia Evaporation Tubular Furnace Chamber Temperature (℃) Oil Pressure (MPa) Ammonium Sulfate Section Tubular Furnace Chamber Temperature (℃) Temperature of Circulating Ammonia Water (℃) Ammonium Sulfate Section Top Temperature of Benzene Removal Tower (℃) Temperature of Circulating Ammonia Water (℃) Saturator Resistance (pa) Top Temperature of Benzene Removal Tower (℃) Current of Circulation Pump Motor (A) Saturator Resistance (pa) Steam Pressure of Benzene Removal Tower (pa) Current of Circulation Pump Motor (A) Preheater Temperature (℃) Steam Pressure of Benzene Removal Tower (pa) Temperature of Insulation Box (℃) Preheater Temperature (℃) Superheated Steam Temperature (℃) Temperature of Insulation Box (℃) Acidity of Mother Liquor (%) Superheated Steam Temperature (℃) Electrostatic Precipitator Voltage (V) Acidity of Mother Liquor (%) Total Steam Pressure (MPa) Electrostatic Precipitator Voltage (V) Ammonium Sulfate Production (bags) Total Steam Pressure (MPa) Volume of Recovered Gas Inlet Ammonium Sulfate Production (bags) Amount of Oil Used for Washing Volume of Recovered Gas Inlet Ammonium Sulfate Production (bags) Amount of Oil Used for Washing Quantity of Tar Sent to Oil Storage Tank (t) Sulfuric Acid Consumption Quantity of Crude Benzene Sent to Oil Storage Tank Quantity of Tar Sent to Oil Storage Tank (t) Sulfuric Acid Consumption Quantity of Crude Benzene Sent to Oil Storage Tank Operation Notes Shift Officer: Operation Notes Shift Officer: Shift: 16:00-0:00 Drum Cooling Section Desulfurization Section Ammonium Sulfate (Ammonia Evaporation) Crude Benzene Section Crude Benzene Section Absorption Pressure Before Machine (pa) Oil Pressure (MPa) Circulating Liquid Flow Rate (m3/h) Amount of Alkali Added during Ammonia Evaporation Gas Temperature Before Final Cooling Tower (℃) Tubular Furnace Chamber Temperature (℃) Absorption Pressure Before Unit (pa) Temperature of Circulating Ammonia Water (℃) Compressed Air Flow Rate into Regeneration Tower (m3/h) Ammonium Sulfate Section Gas Temperature after Final Cooling Tower (℃) Top Temperature of Benzene Removal Tower (℃) Gas Temperature Before Unit (℃) Current of Circulation Pump Motor (A) Sulfur Production (t) Saturator Resistance (pa) Final Cooling Resistance (pa) Steam Pressure of Benzene Removal Tower (pa) Collection Temperature (℃) Temperature of Insulation Box (℃) Ammonium Sulfate (Ammonia Evaporation) Preheater Temperature (℃) Gas Temperature after Benzene Washing Tower (℃) Superheated Steam Temperature (℃) Pressure After Machine (pa) Electrostatic Precipitator Voltage (V) Temperature after Fractionator (℃) Acidity of Mother Liquor (%) Temperature of Lean Oil Going into Tower (℃) Total Steam Pressure (MPa) Fan Motor Current (A) Volume of Recovered Gas Inlet Top Temperature of Tower (℃) Ammonium Sulfate Production (bags) Pressure after Benzene Washing Tower (pa) Amount of Oil Used for Washing Coolant Oil Temperature (℃) Quantity of Tar Sent to Oil Storage Tank (t) Wastewater Temperature (℃) Sulfuric Acid Consumption Oil Temperature at Exit of Tubular Furnace (℃) Quantity of Crude Benzene Sent to Oil Storage Tank Operation Notes Shift Officer:
This should be the operation record for a workshop equipped with a control room