Untitled Document

Trans. No.	Title of Report:	Other Designation:	Location:
L-1	High Pressure Valves.		B9-14
L-2	Comments by Bredtschneider on Needle Valve F-1728.		B9-15
L-3	Vapor Phase Converters.		B9-16
L-4	Comments on 130 Ton Gantry Crane Star Iron and Steel Company, Dwg. 6676.		B9-17
L-5	Operating Directions for the High Pressure Equipment.		B9-18
L-6	Comments on Liquid Phase Converter.		B9-19
L-7	Comments on Hot Catchpot.		B9-20
L-11	Description of an Expansion Engine.		B9-21
L-12	Suggestions for Installing Lens Gaskets in High Pressure Pipe Lines.		B9-22
L-13	Comments on Repair Shop, Repair Pit, and Stall Crane at Louisiana.		B9-23
L-15	Lenses Proposed for Louisiana.		B9-24
L-16	Methane-Steam Reaction at High Pressure.		B9-25
L-17	Bid on 200+/day L. T. C. and Lurgi Plant for Japan.		B9-26
L-19	Gasification of Union Briquettes in Pintsch-Hillebrand Generator.		B9-27
L-20	L. T. C. of Bituminous Coal.		B9-28
L-21	Flowsheet for 240,000 t/ann. DHD Gasoline.		B9-29
L-33A	Suggestions for the Preparation of Coal Paste.		B9-30
L-35	Bredtschneider's Comments on Dwg.-1082-1 with Sketch EDS 159.		B9-31
L-36	Bredtschneider's Comments on Heat Exchangers.		B9-32
L-37	Bredtschneider's Comments on Diaphragm Valves.		B9-33
L-38	Connections in the Coal Stall of the Large Size Installations and the Heat Efficiency.		B9-34
L-39	Gas Purification by Means of Deep Temperature.		B9-35
L-40	Bredtschneider's Comments on Cold Gas Connections to H. P. Vessels.		B9-36
L-41	Study of Pressure Drop in the Coal Stall of the Large Installation.
L-42	High Pressure Viscosimeter by K. Bredtschneider.		B9-37
L-43	Oxygen Plant.		B9-38
L-44	Calculations for the Decision Whether the German Heat Exchangers with 199 Tubes can be Adapted to 30,000 BBL/day installation or will have to be increased.		B9-39
L-45	Low Temperature Purification Plant		B9-40
L-46	Laying out the Preheater with Regard to Starting.		B9-41
L-47	Moisture of Air.		B9-42
L-48	Operating Directions for the Linde-Fränkl Oxygen Plant.		B9-43
L-49	Ball Heater as Water Gas Generator.		B9-44
L-50	Letter: Re. Equipment of 1/2 Coke Oven-Water Gas.		B9-45
L-51	Coal Science.		B9-46
L-52	Layout of the Heat Exchangers of the 30,000 BBL-Plant		B9-47
L-53	Letdown in Stages of the CO₂ Scrubbing Water.		B9-48
L-54	Linde Separation of the Off-Gas of the 30,000 BBL/Day Coal Hydrogenation Plant.		B9-49
L-55	Heat Computations of the Stalls for the Production of 10,000 BBL/Day of Fuel Oil Filtrate.		B9-50
L-56	A Comparison of Heat Utilization in Radiation and Convection Preheaters of a Coal Stall.		B9-51
L-57	30,000 BBL/Day Hydrogenation Plant.		B10-1
L-57A	30,000 BBL/Day Hydrogenation Plant on the Basis of Recalculated Weights of a Converter.		B10-2
L-58	A Cost Estimate of a Liquid Phase Product Cooler for a 30,000 BBL/Day Plant is to be Based on the following Dimensions and Weights.		B10-3
L-59	Data for the Cost Estimation of the Liquid and Vapor Phase High Pressure Coolers.		B10-4
L-60	Laying Out the Preheater of the Vapor Phase Stall of the 30,000 BBL/Day Plant with Reference to Starting.		B10-5
L-61	H.O.L.D. Coolers (Steam Generators) for 30,000 BBL/Day Plant.		B10-6
L-62	Remarks on the High Pressure Coolers of the 30,000 BBL/Day Installation.		B10-7
L-63	Hydrogenation of Middle Oil, or Status of the Recent Research Work on Hydrogenation with a Fixed Catalyst at 700 Atmospheres.		B10-8
L-64	The Linde Installation for 30,000 BBL/Day Project.		B10-9
L-65	Liquid Phase Preheaters for the 30,000 BBL/Day Installation.		B10-10
L-66	Power Consumption in the CO₂ Scrubbing Plant at Various Pressures.		B10-11
L-67	Proposal for Using Product Coolers of the Tube and Shell Type for Large-Scale Hydrogenation Plants.
L-68	Suggested Arrangement of Hairpins in Convection Type Liquid Phase Preheater for the 30,000 BBL/Day Installation.		B10-12
L-69	Emergency Let-Down Tower of the Liquid Phase of the 30,000 BBL/Day Installation.		B10-13
L-70	Capital Requirements for a 700 Atm. Liquid and Vapor Phase Hydrogenation Installation for the Conversion of 430,000 Ton Dry Raw Coal into 220,000 Ton Motor Gasoline per Year.		B10-14
L-71	Assumed Hydrogenation Behavior of Various Coals.		B10-15
L-72	Fuel Oil Production.		B10-16
L-73	Instructions for Opening and Closing the Hot Catchpot, Dwg. D-1007-2.		B10-17
L-74	Instructions for the Assembly and Disassembly of the Vapor Phase Converter, DWG. D-1080-1.		B10-18
L-75	Measuring the Pressure Drop of All the Apparatus in a Stall by Means of Low Pressure Measuring Equipment.		B10-19
L-76	Instructions for the Assembly and Dismantling of the Liquid Phase Converter, DWG. D-1002.		B10-20
L-77	The Composition of the Fractions of the Linde Gas Separation Plant (30,000 BBL/Day).		B10-21
L-78	Determination of the Coal Conversion in the Liquid Phase of the High Pressure Hydrogenation.		P10-22
L-79	Determining the Flywheel of Bredtschneider's Pressure Expansion Engine.		B10-23
L-80	Assumed Hydrogenation Behavior of Coals II.		B10-24
L-81	Product Balance in the Liquid Phase Stall of the High Pressure Coal Hydrogenation.		B10-25
L-82	The Compressibility Factor of the Circulation Gas of the Liquid and Vapor Phase.		B10-26
L-83	Simple Aid in the Determination of the Mean Log Temperature Difference Limited.		B10-27
L-84	Measurements of the Level in the Hot Catchpot of the Liquid Phase.		B10-28
L-85	Nomogram for the Computation of Milking Problems in the Preparation of Coal Paste.		B10-29
L-86	Erosion in the Preheater of the Liquid Phase Demonstration Plant.		B10-30
L-87	Abstract.		B10-31
L-88	Principles of Pressure Expansion in Measuring Apparatus and Other Small Parts of High Pressure Equipment in Operation with Reference to Drawing D-1311.		B10-32
L-89	Start-up Plan and Schedule of the Hydrogenation Demonstration Plant, Louisiana, Missouri.		B10-33
L-90	Temperature Indicating Points for the Control of the Converter Wall Temperatures.		B10-34
L-92	Recording Indicators for the Amount of H.O.L.D. in the Liquid Phase.		B10-35
L-95	Proposed Patent Application for an Expansion Engine.		B10-36
L-96	Temperature Measurement in the High Pressure Stalls by Means of Thermocouples Welded in Tubes.		B10-37