National Library of Energy BETA

Sample records for thermodynamik pfaffenwaldring 38-40

  1. ,"Florida Natural Gas Processed (Million Cubic Feet)"

    Energy Information Administration (EIA) (indexed site)

    Data for" ,"Data 1","Florida Natural Gas Processed (Million Cubic ... 2:38:40 PM" "Back to Contents","Data 1: Florida Natural Gas Processed (Million Cubic ...

  2. Biochemical & Thermochemical High Throughput Characterization of Feedstocks for BETO 2015 Project Peer Review

    Office of Energy Efficiency and Renewable Energy (EERE) (indexed site)

    20 40 60 80 100 120 140 32 34 36 38 40 42 44 46 48 50 52 54 56 58 60 62 64 66 68 70 Frequency Corn Stover Corn Cob Miscanthus Wheat

  3. Biochemical & Thermochemical High Throughput Characterization...

    Office of Energy Efficiency and Renewable Energy (EERE) (indexed site)

    20 40 60 80 100 120 140 32 34 36 38 40 42 44 46 48 50 52 54 56 58 60 62 64 66 68 70 Frequency Corn Stover Corn Cob Miscanthus Wheat...

  4. Appendix A. Reference case projections

    Gasoline and Diesel Fuel Update

    Persian Gulf Share of World Production 29% 29% 31% 32% 35% 38% 40% 42% a Crude and lease condensate includes tight oil, shale oil, extra-heavy oil, field condensate, and bitumen. b ...

  5. 18-24.tex

    U.S. Department of Energy (DOE) - all webpages (Extended Search)

    4 from (1995TI07): Energy levels of 18 F a E x J π ; T K π τ or Decay Reactions (MeV ± keV) Γ c.m. 0 1 + ; 0 0 + τ 1/2 = 109.77 ± 0.05 min β + 1, 4, 5, 6, 9, 10, 12, 13, 15, 21, 23, 24, 25, 29, 31, 34, 35, 36, 37, 38, 40, 41, 42, 43, 44 0.93720 ± 0.06 3 + ; 0 0 + τ m = 67.6 ± 2.5 ps (g = +0.56 ± 0.05) γ 2, 6, 9, 10, 13, 21, 23, 25, 30, 31, 35, 36, 38, 40, 41, 42, 44 1.04155 ± 0.08 0 + ; 1 τ m = 2.55 ± 0.45 fs γ 6, 9, 21, 25, 30, 31, 34, 35, 37, 38, 40, 42, 43 1.08054 ± 0.12 0 -

  6. Microsoft Word - Appendix A (Mar-11 redux)

    Office of Legacy Management (LM)

    ... of the great differences in magnitude across the different floodplain area groupings. ... 0.09 0.52 2.4 5.0 614 38 40.1 17.0 68.0 51.0 35.3 40.1 46.3 12.1 615 34 44.6 0.35 155 ...

  7. Number of Existing Natural Gas Salt Caverns Storage Fields

    Annual Energy Outlook

    34 35 37 38 40 40 1999-2013 Alabama 1 1 1 1 1 1 1999-2013 California 0 1999-2012 Kansas 1 1 1 1 1 1999-2012 Louisiana 9 10 10 10 11 11 1999-2013 Michigan 2 2 2 2 2 2 1999-2013...

  8. U.S. Natural Gas Number of Underground Storage Salt Caverns Capacity

    Energy Information Administration (EIA) (indexed site)

    (Number of Elements) Salt Caverns Capacity (Number of Elements) U.S. Natural Gas Number of Underground Storage Salt Caverns Capacity (Number of Elements) Decade Year-0 Year-1 Year-2 Year-3 Year-4 Year-5 Year-6 Year-7 Year-8 Year-9 1990's 29 2000's 28 28 29 30 30 30 31 31 34 35 2010's 37 38 40 40 39 39 - = No Data Reported; -- = Not Applicable; NA = Not Available; W = Withheld to avoid disclosure of individual company data. Release Date: 10/31/2016 Next Release Date: 11/30/2016 Referring

  9. Lower 48 Federal Offshore Natural Gas Liquids Lease Condensate, Reserves

    Energy Information Administration (EIA) (indexed site)

    Based Production (Million Barrels) Based Production (Million Barrels) Lower 48 Federal Offshore Natural Gas Liquids Lease Condensate, Reserves Based Production (Million Barrels) Decade Year-0 Year-1 Year-2 Year-3 Year-4 Year-5 Year-6 Year-7 Year-8 Year-9 1980's 38 37 38 40 43 1990's 45 44 44 46 47 49 60 70 72 87 2000's 106 101 90 78 74 62 58 58 41 48 2010's 48 40 40 30 32 - = No Data Reported; -- = Not Applicable; NA = Not Available; W = Withheld to avoid disclosure of individual company

  10. California Federal Offshore Associated-Dissolved Natural Gas, Wet After

    Energy Information Administration (EIA) (indexed site)

    Lease Separation, Estimated Production from Reserves (Billion Cubic Feet) Estimated Production from Reserves (Billion Cubic Feet) California Federal Offshore Associated-Dissolved Natural Gas, Wet After Lease Separation, Estimated Production from Reserves (Billion Cubic Feet) Decade Year-0 Year-1 Year-2 Year-3 Year-4 Year-5 Year-6 Year-7 Year-8 Year-9 1970's 5 1980's 5 24 21 19 24 1990's 25 30 34 34 38 40 42 36 35 37 2000's 41 40 43 45 46 33 35 39 35 36 2010's 28 31 22 21 21 - = No Data

  11. Louisiana Natural Gas Liquids Proved Reserves

    Gasoline and Diesel Fuel Update

    295 263 292 280 303 300 1981-2008 Adjustments 15 -8 20 -14 33 -21 1981-2008 Revision Increases 52 54 42 46 49 55 1981-2008 Revision Decreases 79 57 37 51 48 61 1981-2008 Sales 23 32 11 24 42 19 2000-2008 Acquisitions 19 23 15 30 35 19 2000-2008 Extensions 34 38 40 36 36 37 1981-2008 New Field Discoveries 0 0 0 1 0 3 1981-2008 New Reservoir Discoveries in Old Fields 16 6 12 14 10 31 1981-2008 Estimated Production 62 56 52 50 50 47 1981

  12. Pulsed particle beam vacuum-to-air interface

    DOEpatents

    Cruz, Gilbert E.; Edwards, William F.

    1988-01-01

    A vacuum-to-air interface (10) is provided for a high-powered, pulsed particle beam accelerator. The interface comprises a pneumatic high speed gate valve (18), from which extends a vacuum-tight duct (26), that termintes in an aperture (28). Means (32, 34, 36, 38, 40, 42, 44, 46, 48) are provided for periodically advancing a foil strip (30) across the aperture (28) at the repetition rate of the particle pulses. A pneumatically operated hollow sealing band (62) urges foil strip (30), when stationary, against and into the aperture (28). Gas pressure means (68, 70) periodically lift off and separate foil strip (30) from aperture (28), so that it may be readily advanced.

  13. Connecticut Natural Gas Number of Commercial Consumers (Number of Elements)

    Energy Information Administration (EIA) (indexed site)

    Commercial Consumers (Number of Elements) Connecticut Natural Gas Number of Commercial Consumers (Number of Elements) Decade Year-0 Year-1 Year-2 Year-3 Year-4 Year-5 Year-6 Year-7 Year-8 Year-9 1980's 38 40,886 41,594 43,703 1990's 45,364 45,925 46,859 45,529 45,042 45,935 47,055 48,195 47,110 49,930 2000's 52,384 49,815 49,383 50,691 50,839 52,572 52,982 52,389 53,903 54,510 2010's 54,842 55,028 55,407 55,500 56,591 57,403 - = No Data Reported; -- = Not Applicable; NA = Not Available; W =

  14. CMC vane assembly apparatus and method

    DOEpatents

    Schiavo, Anthony L; Gonzalez, Malberto F; Huang, Kuangwei; Radonovich, David C

    2012-10-23

    A metal vane core or strut (64) is formed integrally with an outer backing plate (40). An inner backing plate (38) is formed separately. A spring (74) with holes (75) is installed in a peripheral spring chamber (76) on the strut. Inner and outer CMC shroud covers (46, 48) are formed, cured, then attached to facing surfaces of the inner and outer backing plates (38, 40). A CMC vane airfoil (22) is formed, cured, and slid over the strut (64). The spring (74) urges continuous contact between the strut (64) and airfoil (66), eliminating vibrations while allowing differential expansion. The inner end (88) of the strut is fastened to the inner backing plate (38). A cooling channel (68) in the strut is connected by holes (69) along the leading edge of the strut to peripheral cooling paths (70, 71) around the strut. Coolant flows through and around the strut, including through the spring holes.

  15. Idaho Number of Natural Gas Consumers

    Energy Information Administration (EIA) (indexed site)

    46,602 350,871 353,963 359,889 367,394 374,557 1987-2015 Sales 346,602 350,871 353,963 359,889 367,394 374,557 1997-2015 Commercial Number of Consumers 38,506 38,912 39,202 39,722 40,229 40,744 1987-2015 Sales 38,468 38,872 39,160 39,681 40,188 40,704 1998-2015 Transported 38 40 42 41 41 40 1998-2015 Average Consumption per Consumer (Thousand Cubic Ft.) 390 433 404 465 422 410 1967-2015 Industrial Number of Consumers 184 178 179 183 189 187 1987-2015 Sales 108 103 105 109 115 117 1998-2015

  16. U.S. Lower 48 States Onshore Maximum Number of Active Crews Engaged in

    Gasoline and Diesel Fuel Update

    Seismic Surveying (Number of Elements) Onshore Maximum Number of Active Crews Engaged in Seismic Surveying (Number of Elements) U.S. Lower 48 States Onshore Maximum Number of Active Crews Engaged in Seismic Surveying (Number of Elements) Year Jan Feb Mar Apr May Jun Jul Aug Sep Oct Nov Dec 2000 0 0 41 41 38 43 44 45 43 46 46 48 2001 44 45 45 47 45 42 42 41 39 39 42 41 2002 38 40 35 32 32 32 34 33 37 38 35 31 2003 28 29 28 27 24 25 28 30 30 31 31 32 2004 33 35 35 36 35 39 38 39 40 42 42 41

  17. Idaho Share of Total U.S. Natural Gas Delivered to Consumers

    Gasoline and Diesel Fuel Update

    46,602 350,871 353,963 359,889 367,394 374,557 1987-2015 Sales 346,602 350,871 353,963 359,889 367,394 374,557 1997-2015 Commercial Number of Consumers 38,506 38,912 39,202 39,722 40,229 40,744 1987-2015 Sales 38,468 38,872 39,160 39,681 40,188 40,704 1998-2015 Transported 38 40 42 41 41 40 1998-2015 Average Consumption per Consumer (Thousand Cubic Ft.) 390 433 404 465 422 410 1967-2015 Industrial Number of Consumers 184 178 179 183 189 187 1987-2015 Sales 108 103 105 109 115 117 1998-2015

  18. Indiana Natural Gas Withdrawals from Gas Wells (Million Cubic Feet)

    Gasoline and Diesel Fuel Update

    Year Jan Feb Mar Apr May Jun Jul Aug Sep Oct Nov Dec 1991 21 18 20 19 19 19 19 18 19 20 19 21 1992 15 14 15 14 14 14 14 14 14 15 15 15 1993 17 15 16 16 16 15 15 15 15 17 17 17 1994 9 8 9 9 9 8 9 9 8 9 9 10 1995 4 34 22 42 21 13 22 18 8 21 28 16 1996 14 15 28 33 34 30 30 29 27 33 45 41 1997 38 40 34 34 40 29 30 40 34 39 115 52 1998 37 52 51 45 11 21 85 75 74 69 66 28 1999 76 69 79 70 82 70 66 75 59 52 79 77 2000 75 60 76 77 73 74 85 82 76 77 68 76 2001 83 63 97 97 16 96 102 100 93 111 102 104

  19. Kansas Natural Gas Vented and Flared (Million Cubic Feet)

    Gasoline and Diesel Fuel Update

    Year Jan Feb Mar Apr May Jun Jul Aug Sep Oct Nov Dec 1996 63 63 63 61 62 57 57 55 56 58 59 61 1997 60 55 60 59 62 60 58 54 50 54 54 54 1998 55 50 54 52 52 52 45 48 48 51 49 50 1999 52 44 47 46 46 47 46 46 44 45 44 46 2000 47 43 45 50 45 44 45 45 42 42 41 41 2001 42 37 41 40 41 39 41 41 39 40 39 40 2002 40 36 40 38 40 39 39 39 36 37 36 37 2003 36 32 36 35 36 34 36 36 35 35 34 34 2004 34 32 34 33 34 33 35 34 33 33 32 32 2005 32 30 32 32 32 30 32 33 31 32 31 31 2006 30 27 30 30 30 30 31 32 31 30 31

  20. Pygmy dipole mode in deformed neutron-rich Mg isotopes close to the drip line

    SciTech Connect

    Yoshida, Kenichi

    2009-10-15

    We investigate the microscopic structure of the low-lying isovector-dipole excitation mode in neutron-rich {sup 36,38,40}Mg close to the drip line by means of the deformed quasiparticle random-phase approximation employing the Skyrme and the local pairing energy-density functionals. It is found that the low-lying bump structure above the neutron emission-threshold energy develops when the drip line is approached, and that the isovector dipole strength at E{sub x}<10 MeV exhausts about 6.0% of the classical Thomas-Reiche-Kuhn dipole sum rule in {sup 40}Mg. We obtained the collective dipole modes at around 8-10 MeV in Mg isotopes, that consist of many two-quasiparticle excitations of the neutron. The transition density clearly shows an oscillation of the neutron skin against the isoscalar core. We found significant coupling effects between the dipole and octupole excitation modes due to the nuclear deformation. It is also found that the responses for the compressional dipole and isoscalar octupole excitations are much enhanced in the lower energy region.

  1. Study of the operational conditions for anaerobic digestion of urban solid wastes

    SciTech Connect

    Castillo M, Edgar Fernando . E-mail: efcastil@uis.edu.co; Cristancho, Diego Edison; Victor Arellano, A.

    2006-07-01

    This paper describes an experimental evaluation of anaerobic digestion technology as an option for the management of organic solid waste in developing countries. As raw material, a real and heterogeneous organic waste from urban solid wastes was used. In the first experimental phase, seed selection was achieved through an evaluation of three different anaerobic sludges coming from wastewater treatment plants. The methanization potential of these sludges was assessed in three different batch digesters of 500 mL, at two temperature levels. The results showed that by increasing the temperature to 15 deg. C above room temperature, the methane production increases to three times. So, the best results were obtained in the digester fed with a mixed sludge, working at mesophilic conditions (38-40 deg. C). Then, this selected seed was used at the next experimental phase, testing at different digestion times (DT) of 25, 20 and 18 days in a bigger batch digester of 20 L with a reaction volume of 13 L. The conversion rates were registered at the lowest DT (18 days), reaching 44.9 L/kg{sup -1} of wet waste day{sup -1}. Moreover, DT also has a strong influence over COD removal, because there is a direct relationship between solids removal inside the reactor and DT.

  2. Particle separating apparatus and method

    DOEpatents

    Van den Engh, Gerrit J.

    1999-01-01

    A disposable first tube (68) extends axially through, and is detachably connected to, an annular main body (10'). An input piezo electric element (38) is attached to a first end of the tubular main body (10'). A second, sensor piezo electric element (40) is attached to the opposite end of the main body (10'). A nozzle (20') having a nozzle passageway (110) and a discharge opening (112) is detachably secured to an outlet end of the first tube (68). A second tube (102) within the first tube (68) delivers a core liquid to the nozzle passageway (110). A sheath liquid is delivered through a space in the first tube (68) surrounding the second tube (102). The nozzle passageway (110) forms the core and sheath liquids into a small diameter jet stream. Electrical energy is delivered to the input piezo electric element (38), to vibrate the nozzle (20') and break the jet stream into droplets. The sensor element (40) determines the amplitude of vibration at the nozzle (20') and delivers this information to a control circuit that adjusts the electrical energy input to the input piezo electric element (38) for maintaining a desired amplitude of vibration at the nozzle (20'). The frequency of vibration is determined by the length of the main body (10') between the two piezo electric elements (38, 40). The first and second tubes (68, 102) are disposable and are replaced after a use rather than being cleaned and sterilized.

  3. Particle separating apparatus and method

    DOEpatents

    Van den Engh, Gerrit J.

    1998-01-01

    A disposable first tube (68) extends axially through, and is detachably connected to, an annular main body (10'). An input piezo electric element (38) is attached to a first end of the tubular main body (10'). A second, sensor piezo electric element (40) is attached to the opposite end of the main body (10'). A nozzle (20') having a nozzle passageway (110) and a discharge opening (112) is detachably secured to an outlet end of the first tube (68). A second tube (102) within the first tube (68) delivers a core liquid to the nozzle passageway (110). A sheath liquid is delivered through a space in the first tube (68) surrounding the second tube (102). The nozzle passageway (110) forms the core and sheath liquids into a small diameter jet stream. Electrical energy is delivered to the input piezo electric element (38), to vibrate the nozzle (20') and break the jet stream into droplets. The sensor element (40) determines the amplitude of vibration at the nozzle (20') and delivers this information to a control circuit that adjusts the electrical energy input to the input piezo electric element (38) for maintaining a desired amplitude of vibration at the nozzle (20'). The frequency of vibration is determined by the length of the main body (10') between the two piezo electric elements (38, 40). The first and second tubes (68, 102) are disposable and are replaced after a use rather than being cleaned and sterilized.

  4. Turbine airfoil with controlled area cooling arrangement

    DOEpatents

    Liang, George

    2010-04-27

    A gas turbine airfoil (10) includes a serpentine cooling path (32) with a plurality of channels (34,42,44) fluidly interconnected by a plurality of turns (38,40) for cooling the airfoil wall material. A splitter component (50) is positioned within at least one of the channels to bifurcate the channel into a pressure-side channel (46) passing in between the outer wall (28) and the inner wall (30) of the pressure side (24) and a suction-side channel (48) passing in between the outer wall (28) and the inner wall (30) of the suction side (26) longitudinally downstream of an intermediate height (52). The cross-sectional area of the pressure-side channel (46) and suction-side channel (48) are thereby controlled in spite of an increasing cross-sectional area of the airfoil along its longitudinal length, ensuring a sufficiently high mach number to provide a desired degree of cooling throughout the entire length of the airfoil.