Новокузнецк

Гость

Каталог

Корзина

Поиск

Войти

Гость

Каталог

Корзина

+7(800)707-21-74
Бесплатно по России

Каталог
Книги
Наука. Техника. Медицина
Промышленность
Compendium for the LNG and CNG Practitioner: Liquefied Natural Gas in Application/Справочник для специалистов по СПГ и КПГ: Применение сжиженного природного газа

Compendium for the LNG and CNG Practitioner: Liquefied Natural Gas in Application/Справочник для специалистов по СПГ и КПГ: Применение сжиженного природного газа

Полистать

В наличии Цена за шт.

2970

Итого: 2970.00

Количество

Купить

Акции и скидки Поделиться

Артикул:00-01099133
Автор: W. Hermeling
ISBN: 978-3-658-38258-2
Обложка: Мягкая обложка
Издательство: Springer (все книги издательства)
Страниц: 225
Год: 2024
Вес: 597 г

Описание Отзывы

Книга на английском языке
This book is intended to provide the practitioner, the plant engineer, the investment decision-maker and the plant fitter with technical and economic findings and considerations on LNG and CNG, as well as bio-LNG and bio-CNG, which I was able to gather in general for cryogenic liquefied and compressed gases during my work at Messer Griesheim, now the Messer Group and its subsidiaries. In addition to LNG, many statements also apply to air gases and ultra-pure gases, regardless of whether they are liquid or gaseous.

Contents
1. LNG and Its Thermodynamics
1.1 LNG
1.1.1 What Is LNG?
1.1.2 Biogas: Bio-LNG
1.1.3 Origin of Natural Gas
1.2 Importance of LNG
1.3 Pipeline Gas and Its Significance
References
2 The Most Important Thermodynamic Processes in the Production, Transport and Storage of LNG
2.1 Adiabatic Cooling
2.2 Mixed Condensation
2.3 Relaxation Energy, The Joule-Thomson Effect
2.4 Compression Energy
2.5 The Critical Point
2.6 Thermodynamic Equilibrium
2.7 The Isobar Below the Critical Point
2.8 Liquefaction of LNG
References
3 LNG: From the Source to the End Customer
3.1 Liquefaction at Source and Transport to Hub
3.2 LNG Transport to the End Customer
3.2.1 The LNG Road Tanker
3.3 LNG Fuelling at the End Customer’s Premises
3.4 Closed and Open Hose System
3.4.1 The Open Hose System
3.4.2 The Closed Hose System
3.5 Refuelling from Above
3.6 Refuelling from Below
3.7 Refuelling While Maintaining Process Pressure
References
4 Operational Management
4.1 Continuous Management
4.2 Discontinuous Operation Management
5 LNG Applications
5. 1 LNG Supply Facilities
5.1.1 Operating Principle Module 1
5.1.2 Operating Principle Module 2
5.1.3 Operating Principle Module 3
5.1.4 Functional Principle of Grid Feed-In/Grid Stabilisation
5.1.5 Mobile Emergency Care
5.2 Possibilities of Gas Compression
5.2.1 Gas Compression with Compressor, Cryo-Pump and Liqui-Flow Process
5.2.2 Gas Compression with Cryogenic High-Pressure Piston Pump
5.2.3 Gas Compression with the Liqui-Flow Process
5.3 CNG Filling Stations
5.3.1 Natural Gas Filling Stations with Compressor
5.3.2 Natural Gas Filling Station with Cryogenic Pump
5.3.3 Natural Gas Filling Stations with Liqui-Flow Process
5.4 Satellite Natural Gas Filling Station
5.4.1 Filling of Natural Gas Cylinders, Natural Gas Bundles and Natural Gas Trailers
5.4.2 Energy Requirements of the Satellite Natural Gas Fuelling Station
5.5 Significance of the Holding Pressure Head in the Liqui-Flow Process and for High-Pressure Piston Pumps
References
6 The Thermodynamic Consideration of the Vacuum Insulated Cryogenic Tank
6.1 General Information on the Thermodynamic Function of a Tank
6.1.1 The Thermodynamic Function of the Pump Tank
6.1.2 The Thermodynamic Function of the Refrigeration Tank
6.1.3 The Thermodynamic Function of the Cold Gasifier
6.2 The Design Description of the Vacuum Insulated Tank
6.2.1 General
6.2.2 Tank Designs
6.2.3 Significance of the Tank Pressure
Reference
7 Sensor Technology in an LNG Plant
7.1 Level Measuring Instruments
7.1.1 Differential Pressure Level Gauge
7.1.2 Gravimetric Level Measurement
7.2 Temperature Measurement
7.3 Mass Flow Meters
7.3.1 Coriolis Measuring Device
7.3.2 Mass Flow by Means of Pressure Loss Measurement
8 Equipment of an LNG Plant
8.1 Valves in the Cryogenic Liquid Range and in the Gas Phase
8.2 Check Valve
8.3 Gas Pressure Regulator
8.3.1 Gas Pressure Regulator, Simple
8.3.2 Dual Function Gas Pressure Regulator
8.4 Air Evaporator
8.5 Gas Preheaters in Cogeneration Installations or in Installations with Gas Burners
8.6 Odorization Systems and Odorization
9 Safety Devices
9.1 Safety Valves
9.1.1 Safety Valves (SV) in the System
9.1.2 Safety Shuttle Valve of the Tank
9.1.3 Integrated Safety Shut-Off Valve in Gas Pressure Regulators
9.2 Process Relief Valve on the Tank
9.3 Safety Shut-Off Valve of the Tank
9.4 Setting the Opening Pressures of the Safety Devices on the Tank
9.5 Overfill Protection
9.6 Overfill Protection
9.6.1 Overfill Protection by Gas Pressure Build-Up
9.6.2 Overfill Protection by Gas Pressure Build-Up as Retrofitting
9.7 Exhaust Gas Routing
9.8 Gas Warning Systems
9.9 Sounding Pipes on the LNG Tank
10 Constructive Description of the Hose Couplings for Tank Filling
10.1 Coupling of Open Systems
10.2 Coupling of Closed Systems
10.2.1 Couplings with Dead Space
10.2.2 Couplings Without Dead Space
11 Insulations
11.1 Solid Insulation
11.1.1 Vacuum Panels
11.1.2 Mats with Fibrous Structure
11.1.3 Mats of Rubber Compounds
11.1.4 Foamglas Insulation
11.1.5 Insulations of Polyisocyanurate (PIR)
11.2 Vacuum Insulations
11.2.1 Vacuum Insulation for Containers and Pipes
11.2.2 Vacuum Insulation for Fittings
11.2.3 Vacuum Insulated Hoses
11.2.4 Maintenance and Inspection
References
12 Electrical Grounding
12.1 Protective Earthing of the Installation
12.2 Grounding for Filling
12.3 Functional Earthing During Operation
13 Marked Process Disturbances
13.1 Air in the Hose
13.2 Gas Bubbles in the Liquid Line
13.3 Icing
13.4 Product Does Not Flow into the Pump or into the Pressure Lock of a Liqui-Flow System
13.5 Cryogenic Pump Does Not Deliver
14 System Planning
14.1 Natural Gas Supply System
14.2 Natural Gas Filling Stations
14.2.1 Assembly, Erection and Maintenance
14.3 Execution of Pipe Connections and Valve Connections
14.4 Decision Support for the Selection of the Plant Size of a Liqui-Flow Filling Station
14.5 Cost of an Installation
14.5.1 General Information
14.5.2 Investment or Fixed Costs
14.5.3 Variable Costs
14.5.4 Operating Costs
References
15 Commissioning and Decommissioning of an LNG Plant
15.1 Preparatory Measures for Commissioning
15.2 Filling and Starting Up the System
15.3 Decommissioning of an LNG Facility
16 Training Recommendation
16.1 Recommendation for Training Topics for the Plant Operator
16.2 Topic Recommendation for Personal Protection of the Customer at the Petrol Station
16.3 Recommendation of Topics for Training of On-Site Operational Staff
16.4 Recommendation for Training Topics for Service and Repair Personnel
16.5 One-Man Workstation
References
17 Special Instructions and Precautions
17.1 Protective Clothing
17.2 Contact and Skin Contact with Liquid-Carrying Lines
17.3 Extinguishing a Natural Gas Flame
17.4 Damage Scenarios
17.5 Leaking LNG or Gas
17.6 Influencing the Environment
17.7 Included LNG
References

Оставьте отзыв о товаре