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Process Data set: Steel pipe; Steel pipe (en) en de

Tags Dieser Datensatz ist Bestandteil der ÖKOBAUDAT.
Key Data Set Information
Location DE
Geographical representativeness description The data set represents the country specific situation in Germany, focusing on the main technologies, the region specific characteristics and / or import statistics.
Reference year 2018
Name
Base name ; Quantitative product or process properties
Steel pipe; Steel pipe
Use advice for data set The data set represents a cradle to gate inventory. It can be used to characterise the supply chain situation of the respective commodity in a representative manner. Combination with individual unit processes using this commodity enables the generation of user-specific (product) LCAs.
Technical purpose of product or process This product can be used in construction.
Classification number 8.1.02
Classification
Class name : Hierarchy level
  • oekobau.dat: 8.1.02 Building service engineering / Heating / Heat distribution and dissipation
General comment on data set This data set has been modeled according to the European Standard EN 15804 for Sustainable Building. Results are depicted in modules that allow the structured expression of results over the entire life cycle.
Uncertainty margins 10
Description Product system almost completely covered. Good technological, temporal and geographic representativeness.
Copyright Yes
Owner of data set
Quantitative reference
Reference flow(s)
Time representativeness
Data set valid until 2022
Time representativeness description Annual average
Technological representativeness
Technology description including background system Steel pipe for the installation of heatings and gas supply. According to VDI guideline 2067 for steel pipes an average life span of 40 years can be assumed for heating, gas supply and cold water and 25 years for warm water. Steel production: The preparation of the iron ore includes mainly the crushing. The average iron content in the iron ore is 60%. Pellets are small crystallized balls of iron ore. The pelletisation process consists of grinding and drying, balling and induration followed by screening and handling. The provision of hard coal is described in the respective documentation file (please see link below).  For every fraction the transport to Germany is considered in the data set. The transportation includes all necessary transportation means like ship and where required railway.  The coke oven produces as main product coke out of hard coal. The main by-product resulting from this operation is coke oven gas (COG gas) which is used as energy carrier within the steel production. Further by-products as tar, benzene and sulphur are sold and therefore excluded from the system by allocation to (net) calorific value.  In the sinter plant sinter feed is produced based on the major inputs coke, iron ore and additives. Sintering is an agglomeration process which takes place under high temperatures. The raw materials (fine iron ore, coke breeze, additives) are blended, then the coke breeze is ignited. The result of the sinter process is the so-called sinter cake which has to be broken up, screened and cooled down.  The blast furnace is a closed system into which iron bearing materials (iron ore lump, sinter and / or pellets), additives (slag formers such as limestone) and reducing agents (coke) are continuously fed from the top of the furnace shaft through a charging system. A hot air blast, enriched with oxygen and auxiliary reducing agents (e.g. pulverized coal) is injected providing a counter-current of reducing gases. The air blast reacts with the reducing agents to produce mainly carbon monoxide which in turn reduces iron oxides to metal iron. The main products of the blast furnace operation are hot metal, blast furnace gas (BF gas) and blast furnace slag (BF slag). The BF gas is used as fuel for heating comparable to the COG gas or for electricity production.  The objective in oxygen steelmaking is to burn (i.e., oxidise) the undesirable impurities contained in the metallic feedstock. The main elements thus converted into oxides are carbon, silicon, manganese, phosphorus and sulphur. The purpose of this oxidation process, therefore, are to reduce the carbon content to a specified level to adjust the contents of desirable foreign elements and to remove undesirable impurities to the greatest possible extent. The production of steel by the basic oxygen furnace (BOF) process is a discontinuous process which involves the following steps: transfer and storage of hot metal, pre-treatment of hot metal (desulphurisation), oxidation in the BOF (decarburisation and oxidation of impurities) and secondary metallurgical treatment (e.g. vacuum treatment and adding alloying elements). Within the main step of the oxygen steelmaking, the hot metal feeds together with steel scrap the converter. The main products of the converter are the liquid steel, the converter gas or basic oxygen furnace gas (BOF gas) and the BOF slag. The gas is as well used as energy carrier within the steel production.  Afterwards the continuous casting takes place whereby the liquid steel is cast in continuous strand. The output of the continuous casting process is the slab.  The following operations are two rolling processes: the hot strip mill and the cold rolling mill. In the hot rolling mill the slab is reshaped above the recrystallization temperature. The qualities obtained in this process are e.g. strength and surface quality. During the rolling process the material passes through the furnace and the rolling line. In the furnace the metal is preheated by natural gas. There is no need for an additional warming, if the hot slabs are directly charged into the rolling mill. The forming is done in various rolling frames until the final shape is obtained. The steel scrap in this process are directly recycled.  In the cold rolling mill the material is reshaped below the recrystallization temperature. Thereby a enhanced surface quality, an improved dimensional accuracy as well as a higher strength are achieved. The different process steps are: pickling, the rolling line and the heat treatment.  The cold rolled sheet is transferred to the hot-dip galvanising. The zinc coating is applied by dipping the sheet steel into a hot zinc bath. During the hot-dip galvanising the cold rolled sheet passes the following process steps: preheating furnace (organic impurities are burned off), reduction zone (the sheet is heated to cause recrystallization), cooling and homogenization as well as metal bath (coating of the sheet) and finishing stand. Background system: Electricity: Electricity is modelled according to the individual country-specific situations. The country-specific modelling is achieved on multiple levels. Firstly, individual energy carrier specific power plants and plants for renewable energy sources are modelled according to the current national electricity grid mix. Modelling the electricity consumption mix includes transmission / distribution losses and the own use by energy producers (own consumption of power plants and "other" own consumption e.g. due to pumped storage hydro power etc.), as well as imported electricity. Secondly, the national emission and efficiency standards of the power plants are modelled as well as the share of electricity plants and combined heat and power plants (CHP). Thirdly, the country-specific energy carrier supply (share of imports and / or domestic supply) including the country-specific energy carrier properties (e.g. element and energy content) are accounted for. Fourthly, the exploration, mining/production, processing and transport processes of the energy carrier supply chains are modelled according to the specific situation of each electricity producing country. The different production and processing techniques (emissions and efficiencies) in the different energy producing countries are considered, e.g. different crude oil production technologies or different flaring rates at the oil platforms. Thermal energy, process steam: The thermal energy and process steam supply is modelled according to the individual country-specific situation with regard to emission standards and considered energy carriers. The thermal energy and process steam are produced at heat plants. Efficiencies for thermal energy production are by definition 100% in relation to the corresponding energy carrier input. For process steam the efficiency ranges from 85%, 90% to 95%. The energy carriers used for the generation of thermal energy and process steam are modelled according to the specific import situation (see electricity above). Transports: All relevant and known transport processes are included. Ocean-going and inland ship transport as well as rail, truck and pipeline transport of bulk commodities are considered. Energy carriers: The energy carriers are modelled according to the specific supply situation (see electricity above). Refinery products: Diesel fuel, gasoline, technical gases, fuel oils, lubricants and residues such as bitumen are modelled with a parameterised country-specific refinery model. The refinery model represents the current national standard in refining techniques (e.g. emission level, internal energy consumption, etc.) as well as the individual country-specific product output spectrum, which can be quite different from country to country. The supply of crude oil is modelled, again, according to the country-specific situation with the respective properties of the resources.
Pictogram of technology
Flow diagram(s) or picture(s)
  • abmessungen stahlrohre.jpg Image

Indicators of life cycle

IndicatorDirectionUnit Production
A1-A3
Transport
C2
Waste processing
C3
Recycling Potential
D
Input
  • 1.711
  • 0.03038
  • 0.002875
  • 1.345
Input
  • 0
  • 0
  • 0
  • 0
Input
  • 1.711
  • 0.03038
  • 0.002875
  • 1.345
Input
  • 23.09
  • 0.1203
  • 0.0219
  • -11.79
Input
  • 0
  • 0
  • 0
  • 0
Input
  • 23.09
  • 0.1203
  • 0.0219
  • -11.79
Input
  • 0.2001
  • 0
  • 0
  • 0
Input
  • 0
  • 0
  • 0
  • 0
Input
  • 0
  • 0
  • 0
  • 0
Input
  • 0.001729
  • 0.00001612
  • 0.000005511
  • -0.001062
Output
  • 2.04E-8
  • 3.093E-9
  • 3.338E-10
  • -9.987E-9
Output
  • 0.0281
  • 0.00004417
  • 0.1101
  • -0.02246
Output
  • 0.0002115
  • 0.000003184
  • 2.456E-7
  • 0.000214
Output
  • 0
  • 0
  • 0
  • 0
Output
  • 0
  • 0
  • 0
  • 0
Output
  • 0
  • 0
  • 0
  • 0
Output
  • 0
  • 0
  • 0
  • 0
Output
  • 0
  • 0
  • 0
  • 0

IndicatorUnit Production
A1-A3
Transport
C2
Waste processing
C3
Recycling Potential
D
  • 2.514
  • 0.009056
  • 0.001501
  • -1.559
  • 7.26E-15
  • 1.44E-16
  • 8.336E-18
  • 9.578E-15
  • 0.000727
  • -0.00001417
  • 7.228E-7
  • -0.0004697
  • 0.005364
  • 0.00003799
  • 0.000009533
  • -0.003597
  • 0.0005266
  • 0.000009449
  • 0.000001073
  • -0.0002988
  • 1.626E-7
  • 1.857E-9
  • 1.521E-10
  • 3.711E-8
  • 22.56
  • 0.1123
  • 0.02128
  • -12.33