In oil refining enterprises, different oil refining process would produce a certain amount and quality of wastewater. Based on the tracking model of material flow analysis method, all the water process was integrated into the water balance system, and the optimization model and evaluation index system of the water supply network were established. Taking the oil refinery in China as an example, the water network model of the oil refining production process was constructed, and the minimum water consumption problem of the current water system was determined. The method was optimized and evaluated. The results showed that the fresh water consumption could be reduced by 26.90% and the sewage discharge could be reduced by 84.42% after taking the water system optimization measures. Waterenvironmental efficiency increased by 15.34%.

        The carbon flow model was established based on Substance Flow Analysis (SFA) and the factors that cause the carbon emission were analysis by mathematical programming. The evaluation indicators were defined in order to evaluate the carbon flowing of TDCS. The results show that the main form of carbon emission is the carbon gases discharged to the environment for TDCS. The main sub-process of carbon emission is the preheating subprocess. And the carbon emission increases with the increasing of fuel consumption and C/H ratio, which influence the carbon emission most.

In order to operate the town polyethylene gas pipeline safely and reduce the operational risk, the possible accidents were analyzed that the town gas polyethylene pipe could occur and its reasons. Using fault tree analysis method, both the fault tree model and its sub fault tree model of the town polyethylene gas pipeline were established. Through the calculation of the minimum cut sets, the minimum path sets and the structure importance of it, the possible malfunctions of the town polyethylene gas pipeline and the reasons were analyzed. The research results show that the failure of town polyethylene gas pipeline had a larger threat, and the threat of pipeline auxiliary facilities failure was less. Among the reasons of pipeline failure, the influence of the outside interference was the largest|the scratches and defects of the pipeline had a minor influence|and the aging pipes and stress effect on the pipeline had the least influence on the pipeline accidents.

The steam quality on the top of oil well is one of the important parameters during the thermal oil, and calculation software for the steam quality was developed by VB6.0,and the accuracy of the software was validated by experimental measurement data calculation. The impact the structural parameters (pipe diameter、the thickness of thermal insulation layer)and operating parameters(steam temperature、steam pressure and pipe inlet steam flow) of the steam quality and its change rule were analyzed systematically. Research results show that the steam quality on the top of oil well increased with the increment of the thickness of thermal insulation layer and pipe inlet steam flow and decreased with the increased of the pipe diameter、steam temperature and steam pressure. The thickness of thermal insulation layer was of the greatest impact among such factors, when the thickness of thermal insulation layer was greater than 60 mm and less than 80 mm, and each time the thickness of thermal insulation layer increased 20 mm, the steam quality increased 0120%.

The heavy oil electric heat pipe tracing twodimensional unsteady model was established to analyze the influence and the laws of heavy oil pipeline safety shutdown time under the thickness of pipe insulation, the number of heating pipes and location parameters. The results show that in the case of a single tube with heat, when the pipe thickness was respectively 60, 70 mm, and 80 mm, corresponding security shutdown time was about 26, 30 h, and 34 h| in the case of double pipes heating, the change of the angle between the two tubes had the smaller impact on the safety shutdown time, and the safety shutdown time was about 36 h.

For high temperature steam vapor transport in the buried pipeline causes heat loss and leads to energy waste problems，several factors affecting heat loss were analyzed. Steam pipeline of physical model and mathematical model was established to simulate the different steam temperatures，different buried depth and temperature distribution under different insulation thickness. And temperature distribution pipeline and the surrounding soil were calculated and analyzed under different conditions. The results show that the heat loss of buried steam lines with the steam temperature, buried depth, changed the thickness of the insulating thickness changes，and the biggest affect of the heat loss was the insulation thickness. When the insulation thickness was from 40 mm to 80 mm，the heat loss per unit length declined 110.591 W/m，and the thermal effect was smaller and smaller .

The total idea for waste water controlling was described and then the emission concentration limited of the chemical oxygen demand（COD）and the ammonia nitrogen（NH3N）for the Jinsha River, the Luanhe River and Dalinghe River were calculated respectively by twodimensional water quality model. The results show that the COD emission concentration limits of the three rivers were under the current standards. However, the NH3N emission concentration limits were all closed to or above the standards; the recommended COD and NH3N emission concentration limits were no more than 60 and 15 mg/L, respectively.

Considering the large resource of low temperature waste heat in heavy reservoir thermal recovery process, the technology of recover waste heat in oil field was used for heating pipeline in heavy oil transportation. The model of dynamic simulation system of the technology was established by MatlabSimulink, and the heating efficiency of the technology system was obtained. The results of the study show that the heating temperature of system can achieve 75 ℃, satisfied with the temperature requirements of heating water in heavy oil transportation, and the heating coefficient of system is 3.5. Based on this, through the analysis of the energy that the established system model can save standard coal 17 t/a better than boiler heating model, to reduce the discharge of pollutants in the air 0.714 t/a, the system has a large economic and environmental benefits.

The wasting of the superheated steam or heating the oil reservoir not sufficiently might be caused by the uncertainty of steam injection period during the steam soak, therefore, and a two-dimensional, unsteady state mineshaft-stratum-oil reservoir mathematical model was established, and the temperature fields of the stratum and the oil reservoir were analyzed. Furthermore, the influences of steam injection period to the heat affected radius during the steam soak were discussed. The results show that the heat affected radius of the oil reservoir increases with steam injection period duration and reaches the maximum when the steaming for 5 d, then nearly no longer changed after that. The heat in the oil reservoir began to transfer to the stratum when the steaming for 3 d, and the temperature fields of the stratum and the oil reservoir are nearly the same for 6 d. The steam injection period should be controlled in 4~5 d during the steam soak.