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In the high pressure of polymerization of ethylene homopolymer or copolymers conditions in the reactor may become unstable leading to the decomposition (“decomp”) of the reaction mixture. Monitoring temperature excursions traveling through the reactor over close thermocouples (a roller) to detect ch

In the high pressure of polymerization of ethylene homopolymer or copolymers conditions in the reactor may become unstable leading to the decomposition (“decomp”) of the reaction mixture. Monitoring temperature excursions traveling through the reactor over close thermocouples (a roller) to detect changes in the mean temperature and the moving temperature front for a group of thermocouples detects conditions potentially leading to a decomp.

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1. A method to control process temperature conditions leading to an increased likelihood of decomposition of a mixture of 100 to 60 weight % of one or more C2-8 alpha olefins and 0 to 40 weight % of one or more compounds selected from the group consisting of vinyl acetate; C3-6 ethylenically unsatur

1. A method to control process temperature conditions leading to an increased likelihood of decomposition of a mixture of 100 to 60 weight % of one or more C2-8 alpha olefins and 0 to 40 weight % of one or more compounds selected from the group consisting of vinyl acetate; C3-6 ethylenically unsaturated carboxylic acids and C1-4 alkyl esters thereof in the presence of one or more initiators selected from the group consisting of oxygen, hydrogen peroxide, organic peroxides, persulfates, perborates, percarbonates, and organic azo compounds at pressures from 80 to 310 MPa and temperatures from 130 to 350° C. in a tubular reactor having a length from 200 m to 1500 m and a diameter from 20 mm to 110 mm having n thermocouples along the length of the reactor where n is a whole number between 100 and 350 comprising: i) operating the reactor at the above conditions to produce a product and taking from 10 to 100 temperature readings per second over a period of time of not less than thirty seconds and not more than 5 minutes from each thermocouple to a microprocessor programmed to calculate as based on said reading from said thermocouple the mean temperature, the standard deviation (ó), the mean temperature plus from three standard deviations (3ó) to the mean temperature plus from three to six standard deviations as the control limits for each thermocouple, the absolute temperature difference between sequential measurements to determine a moving range and to compare those values to the control limits over two to five adjacent thermocouples out of said n thermocouple;ii) calculating with the microprocessor said mean temperature, standard deviation (ó), the mean temperature plus from three standard deviations (3ó) to the mean temperature plus six standard deviations (6ó); the mean temperature minus three sigma (3ó), the control limits for each thermocouple; and a moving range of said temperature reading values for each thermocouple for that given time period wherein said microprocessor is further programed to preform the following steps;iii) for the next sequential time segment covering not less than 30 seconds and not more than 5 minutes providing the microprocessor temperature readings at a frequency of not less than 10 Hertz to determine;iv) , if: a) the temperature is between 3d and 6d above the established mean temperature; andb) the moving range exceeds a predetermined threshold between 0.5 and 1.3° C., that extends across two to five adjacent thermocouples; andv) if both conditions (a) and (b) are not met, for the current segment of data;vi) if a temperature excursion between 3d to 6d above the mean temperature and the moving range also exceeds the predetermined threshold between 0.5 and 1.3° C. for a given thermocouple that extends across two to five adjacent thermocouples using the microprocessor to increase one or more of the coolant temperature and the inlet temperature of the reactants by not less than 5° C. or decrease the reactor peak temperature. 2. The method according to claim 1, wherein said microprocessor is further programed to control the predetermined threshold against which the moving range is compared is between 0.7 and 1° C. 3. The method according to claim 2, wherein said microprocessor is further programed to control the reaction temperature is from 150 to 340° C. 4. The method according to claim 3, wherein said operating conditions include the pressure is from 200 to 300 MPa. 5. The method according to claim 4, wherein in step i) not less than 450 measurements are provided to establish the mean reaction temperature and standard deviation. 6. The method according to claim 5, wherein in step ii) the temperature excursion is observed over not less than 3 adjacent thermocouples out of said n thermocouples. 7. The method according to claim 6, wherein said microprocessor is further programed to control the mean temperature is from 200 to 340° C. 8. The method according to claim 7, where in the mixture comprises 100 to 80 weight % of one or more C2-8 alpha olefins and 0 to 20 weight % of one or more compounds selected from the group consisting of vinyl acetate, and C3-6 ethylenically unsaturated carboxylic acids and C1-4 alkyl esters thereof.