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This post was last edited by hu*aogang on 2010-3-23 at 16:28. Does any member have questions related to the Luqi pressurized gasification 800# gas-water separation unit? I need it urgently, thank you
Gas-water separation – Test paper for the first week of March Name: _____________ Score: ____ I. Fill in the blanks (60 points) 1. The operating temperature of the final oil separator in PID10 is ___________. 2. The instrument tag numbers on the nitrogen pipeline at PID10 F623A25A are ___________, ____________. 3. In PID08, port S18 of the oil separator denotes ________, S14 denotes ________, S6 denotes _______, and S15 denotes ____________. 4. The temperature of the fluid inside TPD623A002 in PID01 after passing through C623A01ABC is ________; the temperature of the fluid flowing in the shell side is ________, and the shell-side fluid goes to ________ work station. 5. The function of the low-pressure steam supplied to the coke filtration basket via PID10 is ____________. 6. There are two spring-loaded safety valves in the inlet pipeline of C623A02, through which the dust-containing gas and water coming from C623A01 enter; their tag numbers are __________, ___________. 7. The pipeline that carries fluid to the reflux gas and water distributor SPP623A03A via PID10 is labeled ____________________. 8. The function of a steam trap is _______________________. 9. The pipeline that carries oil-containing gas and water to the oil separator via PID08 is labeled ______________________________. 10. ST stands for ____________, SC stands for ___________, SV stands for ___________, _______________. 11. During the initial startup, when the pressure of the dust-containing gas and water coming from unit 606 is greater than 0.4 MPa, it enters _______________; when the pressure is less than 0.4 MPa, it enters ________________. 12. The pipeline CWS623A013, which connects the circulating water supply CWS623A005 to the circulating water return CWR623A005 in PID02’s circulating water system, serves the purpose of _______________. 13. PID02’s PICA623A06 is used to control ______ pipelines, with the fluid flowing into 4 units of ___________. 14. What kinds of impurities are present in gas and water? There are various impurities such as _, _, _, _, etc. 15. During the washing and cooling of raw coal gas, coal gas water with various components in , , , and other states is formed. 16. The specific gravity difference between tar and water at 92°C is , while the specific gravity difference between oil and water is greatest at . The greater the difference in specific gravity, the easier it is. 17. In PID05, the S28 of the primary tar separator is the inlet, and its pipeline tag number is . The outlet for the dust-containing tar in PAD is , while the pure tar from PAC goes to the relevant equipment. 18. PID07: Specify the location number of the oil-containing gas water pipeline corresponding to work order No. 609; for the oil-containing non-steam water expansion vessel F623A21A, port S7 is _________. II. Term Explanation (10 points) 1. Flashing of dissolved gases? 2 What is the definition of coal tar? III. Short-answer Questions (30 points) 1. Describe in detail, with reference to PID08, the flow process of the expanded gas from the dust-containing gas and water expanded gas safety water seal F623A27AB to F623A12A 158025954@qq.com
Water separation – Exam in the third week of March. Name: Score: I. Fill in the blanks (1.5 points each) 1. When the vaporization furnace’s pressure is raised to 2.0 Mpa, the ____________ pipeline is connected to the dust-containing gas water pipeline in order to put it into use. 2. To supply high-pressure jet gas water to unit 609# and receive the oil-containing gas water from that unit, the J623A02 pump needs to be started; ____________ must also be put into use. 3. The steps for starting the J623A02 pump are as follows: Open the valve, then open another valve; once water starts flowing, close that valve. Start the J02 pump, and after the flow rate stabilizes, slowly open another valve. Once water starts flowing, open the outlet valve. Close that valve once the pressure reaches 1.8 Mpa. 4. When filling the cooling water into the dust-containing gas-water cooler with C623ABCD02ABCR, open the valve first; once water flow is established, open another valve and then close it. 5. During the initial startup process for filling the liquid level in the oil-containing gas-water system, the sequence of operating the filling equipment is as follows. 6. F26 should be backwashed once a day; when the liquid level in F05 rises above the set limit, start the pump to send fluid to F24. 7. The working principle of the gas-water separation unit relies on the differences between various components, thereby separating oil and dust-containing tar from the gas water mixture. By utilizing the principle that decreasing pressure reduces the solubility of gases in liquids, the gases such as , , and others dissolved in coal gas water are separated through flash depressurization. 8. Control the temperature of the gas and water at the CO2 outlet to prevent emulsification of the gas and water inside the separator, which could affect the separation efficiency. If emulsification needs to be eliminated through temperature adjustment, it is possible to mix certain components together and feed them into F24 to improve the separation effect. 9.609# and 613# have stopped supplying oil-containing gas, water, gas water, and condensate to 623#; the boundary valves leading to 623# were closed to prevent any leakage. N2 was introduced into the lines carrying expanded gas, thereby purging the entire pipeline until it was confirmed that the outlet gas contained no such substances. 10. For parking the F22 and F21, when discharge is required, open the bottom valves of F21 and F23. 11. When stopping F24 and F23, open the valve used to purge the pipeline, purge F24, and close it once it is satisfactory. 12. When stopping the F25, close the internal pipelines and external valves. 13. In accident handling, the expansion of oil-containing gas and water to the pressure in the expansion gas cooler lines is caused by air leakage. 14. The fill level in F623AD03 should be maintained at above ________ m. 15. At the utility station, fresh water, utility air, and N2 are released for a short period before being shut off; the purpose of this is __________________. 16. _________ water is used to fill the levels in systems containing oily gas and water, while ________ water is used for systems containing dusty gas and water. 17. When filling F623ABCD01 and F623ABCD02, if freezing is possible, ________________ must be added to their bottoms. 18. After the equipment has been installed or repaired and put into operation, the operators inspect the interior of the equipment to check for any _______________ and ________________. 19. The utility media include ___________, __________, _________, _________, ___________. 20. Before filling the levels in equipment #623, it is necessary to first ensure that all blind flanges and valves are in the _________ position. 21. The fill level in F623AD03 should be maintained at above ________ m. II. Short answer questions 1. Describe the steps involved in filling the primary tar separator F24 (14.5 points) 2. Please write down the worker numbers in the gas generation workshop along with their corresponding names (15 points)
Water Separation – Test Paper for the Second Week of March Name: ____________ Score: ___________ I. Fill in the blanks 1. The pure tar from the primary tar separator is sent to F62306 through the _______________________ pipeline. 2. The oil from _____________________, _________________________, and ___________________ devices is sent to F62307. 3. The reflux pipeline for F62306 is the ________________________; the reflux outlet is ________. 4. In F62306, S16 is ___________, while S4 is _______________. 5. The water used for backwashing is pumped from ________________ by the backwashing gas water pump to the bottom of the dual-media filter. The dual-media filter is backwashed every ____ hours. 6. The backwash gas and water, that is, the slurry, is collected in a slurry tank and then sent to __________ using __________ for further treatment. 7. The pipeline tag number for PID14, which is used for backwashing the gas and water, is ___________________________. 8. The function of the exhaled air coming from F26 in PID16 is ___________________________. 9. The pipeline leading from PID17 to the gas and water storage tank before the dual-media filter is ___________________________. 10. The pipeline leading to F24 after being pumped by pump J07 is _______________________________. 11. The instrument tag numbers for the pressure difference of bed F26 are ___________, _______________. 12. PID16: Flushing tank outlet S4 ______________ S6___________ S3 _____________. 13. PID16: Level indication switch alarm instrument on F05 ___________________. 14. PID10 comes from the initial tar, enters the final oil separator, is pumped to the gas cooler, passes through the dual-media filter, and ultimately reaches its destination. 15. What is the function of the unprocessed gas and water distributor and the recycled gas and water distributor? 16. PID11 final oil separator F25’s S13, S9A-D. 17. The connecting pipeline between the first and second buffer tanks of PID12 is , and its function is . 18. PID13 gas-water cooler, S7. S5. 19. The main function of the final oil separator F25 is . II. Write down the corresponding medium or code based on those given. Wastewater containing ether: DPH; HEW: Aqueous solution of dilute phenol: LAV; PHW: DIS: GS: DIG: Oil: TPH: TPD: Pure tar: Top outlet of acid removal tower __________ Bottom outlet of acid removal tower __________ Top outlet of ammonia removal tower __________ Bottom outlet of ammonia removal tower III. Term explanations 1. What is extraction? 2 What is the function of the deacidification tower? IV. Essay Questions 1. Why is backwashing necessary for dual-media filters? 2. Draw the ammonia condensation process and the non-condensable gas process at the top of the E02 deacidification tower (block diagram) E02 Ammonia at the top of the tower; C09. V. Short-answer questions: 1. Briefly describe how to control the operating temperature at 40–70°C in the F25 final oil separator
Are there any answers to the questions above?
If there are answers and drawings, could you send them over? So that everyone can learn**
Why are your designations different from ours? If sending it again, there’s no need to mention the tag number; just state the names of the equipment, valves, and pipelines.