HGJ 3-1986 Technical Regulations for Energy-saving Design of Synthetic Ammonia HGJ3-1986 Standard download decompression password: www.bzxz.net

Ministry of Chemical Industry of the People's Republic of China
Design Standards
Technical Regulations for Energy-saving Design of Synthetic Ammonia
HGJ3-86
(Trial)
Standard Stable Network
u.btsoro.com1 Technical Regulations for Energy-saving Design of Large-scale Synthetic Ammonia Plants1.1 Total
1.2 Comprehensive Energy Consumption Index
1.3 Energy Consumption Index of Main Processes
1.4 Energy-saving Measures
2 Technical Regulations for Energy-saving Design of Small and Medium-sized Synthetic Ammonia Plants2.1 General Purchase
2.2 Energy Saving Measures
Appendix: Unified Method and Formula Compilation Instructions for Energy Consumption Calculation
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Ministry of Chemical Industry of the People's Republic of China
Design Standard
Technical Regulations for Energy Saving Design of Synthetic Ammonia
HGJ3-86
(Trial)
Standard Grant Network
"Technical Regulations for Energy Saving Design of Synthetic Ammonia" is a design standard approved and promulgated by the Ministry of Chemical Industry for trial implementation. The contents of this regulation include: Technical Regulations for Energy Saving Design of Large Synthetic Complex Units: Technical Regulations for Energy Saving Design of Small and Medium-sized Synthetic Complex Units: Annex and Compilation Instructions.
This regulation was edited by Wuhan Chemical Engineering Company of China. The compilers were Lin Xiyuan, Xi Xinghan, Ran Chonghui Guozhi, the reviewer was Chen Daosanzhi, and the reviewer was Chen Yizhi. Standard exchange network m, bztoo.cem chemical
Design standard
Technical regulations for energy-saving design of synthetic ammonia
Editor: Wuhan Chemical Engineering Company, China Approved by the Ministry of Chemical Industry
January 1987
Design standard
HGJ3-86
Page 1
1 Technical regulations for energy-saving design of large-scale synthetic ammonia plants 1.1 General
Total 14 pages
1.1.1 Energy is an important material basis for my country's socialist modernization drive. Now and in the future, the ministry must implement the policy of giving equal importance to development and conservation of energy. 1.1.2. These regulations apply to the design of new construction, reconstruction and expansion projects of large-scale synthetic equipment. 1.1.3 The comprehensive energy consumption level is divided into the first-level energy consumption standard, the second-level energy consumption index and the third-level energy consumption index. New projects should try to reach the first-level energy consumption index, which should not be higher than the second-level energy consumption index. Reconstruction projects should try to reach the second-level energy consumption index. Expansion projects should reach the second-level energy consumption index, which should not be higher than the third-level energy consumption index. 1.1.4 New energy-saving processes, technologies and high-efficiency equipment should be adopted. Outdated processes with high energy consumption and electromechanical products and equipment that have been announced to be eliminated by the state should not be adopted. 1.5 Attention should be paid to the selection of energy types, reasonable use of energy, comprehensive utilization of process heat energy, multi-level utilization of high-level heat energy, reasonable use of waste heat, waste pressure, condensate, etc., to improve the overall thermal efficiency. 1.1.6 Energy consumption detection and control instruments should be set up in the design, and the level of automatic control should be continuously improved. 1.1.7 Strive to improve investment efficiency and shorten investment payback period 1.1.7.1 The investment of newly built large-scale synthetic nitrogen plants shall be calculated according to the static payback period, which shall generally not exceed five years. 1.1.7.2 The reconstruction project shall save 41.888×10 coke (19 million kcal) per month, and the investment shall be less than 1,000 yuan. 1.1.7.3 When large-scale synthetic ammonia plants using oil as raw material and fuel are converted to coal instead of oil, the investment shall be less than 50 yuan per year to replace one ton of oil (including light oil, diesel, and heavy oil). 1.1.8 The feasibility study report and preliminary design of new and large-scale technical transformation projects shall add chapters on energy conservation and rational utilization. 1.1.9 In addition to the implementation of these regulations, energy-saving design shall also comply with relevant regulations and specifications issued by the state. 1.2 Comprehensive energy consumption indicators 1.2.! The three-level indicators of comprehensive energy consumption for energy-saving design of synthetic nitrogen production with different raw materials formulated in this regulation are shown in Table 1, 2-1.1.2.2 During the "Seventh Five-Year Plan" period, new plants using natural gas or light oil as raw materials should not exceed the second-level indicators, and rebuilt plants and expanded plants should try to reach the second-level indicators. 1.2.3 New plants using heavy oil and coal as raw materials should not exceed the second-level indicators. On the basis of the existing technological level, new plants designed in the late 1990s should further make full use of energy to achieve the first-level indicators of this regulation. 1.2.4 Continuously adopt new processes and technologies. New plants designed in the 1990s using natural gas and light oil as raw materials should meet the first-level indicators of this regulation. 1.3 Energy consumption indicators of main processes
Energy utilization of large-scale synthetic ammonia plants, in terms of saving materials and power, is mainly the comprehensive 23
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HGJ3-86
Total 14 pages
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'6~8'a
D'0P~8\8
Standard industry data science competition fee download|| tt||HGJ3-86
, Page 3
Total 14 pages
Combined utilization, total power consumption is extremely small (some factories are self-sufficient in electricity), the energy utilization of the entire factory is very complex. When different process flows are adopted, the consumption of each section is not interlaced, and it is not convenient to list the comprehensive energy consumption indicators by section. Therefore, the following window lists the energy consumption indicators of raw materials, fuel, water, electricity, and steam in each process of our factory's current production process. 1.3.1 Comprehensive utilization of natural gas as raw material Energy index of main process of nitrogen forming device () Raw material consumption (in tons):
Section air consumption Nm8
Heat mass k (kcal)
23.78x10(5.68x15*)
(2) Natural gas consumption (in tons of nitrogen):
Heat gas consumption Nm
Boiler 16.7
Heat value kl (keal)
15.95x10(3.81 xi0°)
（3，get six spectrum distances (in hours):
soft water consumption kg
calorific value k（keal)
1.24X10°(0.297X10°)
（）electric energy consumption (in hours)
cooling tower
electric spark kWh
（5）cooling part consumption:
calorific value kl（keal)
7.83X10* (1.87X10°)
1.47X10*(0.352X10°)
Cooling water consumption in each process
Electrification
Synthesis, defreezing
Modification of water tower
Study of water
Run/hour
(6) Steam consumption (unit: kg/h) see 1.3-2 heat position × 100 box J/h
23,634
1.3.2 Energy consumption index of main processes of large-scale synthetic nitrogen plant using oil as feed Standard 1.3.2,1 Raw material consumption (in tons of ammonia): Section bay kg. Light oil kg
Gas cargo 743.9
Carbon black return
Light oil used to blacken water with a high rate of embedding
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Heat value kJ (keal)
30.563X10(7.3X10°)
Discounted standard package (g)
Standard coal (5g)
Discounted standard package (kg)
New standard coal (k3)||tt| |Table 1,3-1
(×10ckcal/h)
Converted to standard coal gwww.bzxz.net
0.205×10*(0.049×100)
HGJ3-86
Total 14 pages
Page 4
689°8
Can/1001x
Da/asg
(u/6x).
：872o
Hecheng Refrigeration
De-longning Conversion Section||t t||All kinds of standard industry data are free to get off
Standard net change
HGJ3-86
1.3.2.2 Fuel consumption (in terms of nitrogen consumption): Section heavy alcohol kg
Boiler 441.4
Seal oil*kg
Heat value kl (kcal)
Page 5
19.469×10（4.65×10\)
, seal does not need 0 zero final, adjust the production, start and work with inflammatory shooting system teaching station. 1.3.2.3 Water tray (m%h):
High-temperature collection
One-step chemical conversion
Acid injection gas tax inspection
Nitrogen synthesis
Nitrogen refrigeration
Urban government education
Boiler feed water and steam system cleaning
Raw water treatment and pure water preparation
Refrigeration equipment
Power generation equipment
Instrument air discussion
Emitter skin water recovery
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Total 14 pages
Discount ticket g
Page 6
Total 14 pages
Electricity consumption (kWh/h):
Each process
Black recovery
Oxygen conversion
Integral gas removal
Ammonia synthesis
Good refrigeration
Model and full transmission Supply
Steel guard water and steam system control
Raw water treatment and pure water preparation
Cooling tower equipment
Power generation equipment
Air source
Recycled waste water
Power meter and lighting
Number of factory meters
Indicator
HGI3-86
Electricity consumption meter
HGJ3-86
1.3.2.5 Steam and steam condensation wave (tons/hour): each workstation
steam elimination
zhifan kg/cu (bag)
swimming fish maw
en room collection
carbon exchange
digital gas removal
paper synthesis
effect cooling department
cha area and treatment and exploration
furnace feed water and new energy institute
raw water treatment and integrated water preparation
cooling department equipment|| tt||AC equipment
Only Haikong gas management
Comfort recovery spot water
Anchang accounting
Note, () is the leveling cooling liquid
100 overheat
(465C)
Including 100 yuan/cm (table) Minghe Shengqi 100
Total 14 pages
Cooler received
(24,79)
1.3.3 Used as raw materials Energy flow standard of large-scale synthetic driving equipment of a set of strange furnaces 1.3.3,1 Raw material consumption (in tons of oxygen): Section raw coal kg
Heating value (kcai)
32.20×10*(7.69×10)
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Page 8
Total 14 pages
Fuel consumption (in tons of ammonia):
Raw Butterfly kg
Heat value (kcan)
HGJ3-86
14.61×10*(3.49×10)
Power consumption and water consumption are shown in the following table:
Original Fan Point Preparation
Gas Water High Cold Welding
Long Temperature A Chemical Washing
Methane Steam Conversion
Red Synthetic Medical Code
Gas Water Suspected Tar and Light Flag
Aeration Water Device| |tt||Gas water nitrogen recovery
Coal traces and coal valley treatment
Biochemical treatment
Cold plastic water system
Cold and desalted water treatment
Power generation unit
Only air
Each condensate level
Show construction area
Equivalent standard coal (kg)
Electricity consumption kWh/h
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Water permeability 3/h
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