The LPMEOH process was conceived and patented by Chem Systems Inc. in 1975. Initial research and studies on the process focused on two distinct modes of operation. The first was a liquid fluidized mode with relatively large catalyst pellets suspended in a fluidizing liquid, and the second was an entrained (slurry) mode with fine catalyst particles slurried in an inert liquid. The development of both operating modes progressed in parallel from bench scale reactors, through an intermediate scale lab PDU, and then to the LaPorte PDU in 1984. The slurry mode of operation was ultimately chosen as the operating mode of choice due to its superior performance
The project involves the construction of an 80,000 gallons per day (260 TPD) methanol unit utilizing...
The Liquid Phase Methanol (LPMEOH{trademark}) demonstration project at Kingsport, Tennessee, is a $2...
The commercial reactor type proposed for the liquid phase methanol synthesis (LPMeOH™) process is a ...
In April 1987, Air Products started the third and final contract with the US Department of Energy to...
During this period the Work Breakdown Structure Dictionary was established. Task 1 was completed wit...
A fluid dynamic study was successfully completed in a bubble column at DOE's Alternative Fuels Devel...
The project involves the construction of a 260 tons-per-day (TPD) or 80,000 gallon per day methanol ...
The project involves the construction of an 80,000 gallons per day (260 TPD) methanol unit utilizing...
The Liquid Phase Methanol (LPMEOHTM) Demonstration Project at Kingsport, Tennessee, is a $213.7 mill...
The Liquid Phase Methanol (LPMEOH{trademark}) Demonstration Project at Kingsport, Tennessee is a $21...
The Liquid Phase Methanol (LPMEOH{trademark}) Demonstration Project at Kingsport, Tennessee, is a $2...
The Liquid Phase Methanol (LPMEOW) Demonstration Project at Kingsport, Tennessee, is a $213.7 millio...
During this quarter, the third draft of the Topical Report on Process Economics Studies was issued f...
he Liquid Phase Methanol (LPMEOW) Demonstration Project at Kingsport Tennessee, is a $213.7 million ...
The Liquid Phase Methanol (LPMEOEP") Demonstration Project at K.ingsport, Tennessee, is a $213.7 mil...
The project involves the construction of an 80,000 gallons per day (260 TPD) methanol unit utilizing...
The Liquid Phase Methanol (LPMEOH{trademark}) demonstration project at Kingsport, Tennessee, is a $2...
The commercial reactor type proposed for the liquid phase methanol synthesis (LPMeOH™) process is a ...
In April 1987, Air Products started the third and final contract with the US Department of Energy to...
During this period the Work Breakdown Structure Dictionary was established. Task 1 was completed wit...
A fluid dynamic study was successfully completed in a bubble column at DOE's Alternative Fuels Devel...
The project involves the construction of a 260 tons-per-day (TPD) or 80,000 gallon per day methanol ...
The project involves the construction of an 80,000 gallons per day (260 TPD) methanol unit utilizing...
The Liquid Phase Methanol (LPMEOHTM) Demonstration Project at Kingsport, Tennessee, is a $213.7 mill...
The Liquid Phase Methanol (LPMEOH{trademark}) Demonstration Project at Kingsport, Tennessee is a $21...
The Liquid Phase Methanol (LPMEOH{trademark}) Demonstration Project at Kingsport, Tennessee, is a $2...
The Liquid Phase Methanol (LPMEOW) Demonstration Project at Kingsport, Tennessee, is a $213.7 millio...
During this quarter, the third draft of the Topical Report on Process Economics Studies was issued f...
he Liquid Phase Methanol (LPMEOW) Demonstration Project at Kingsport Tennessee, is a $213.7 million ...
The Liquid Phase Methanol (LPMEOEP") Demonstration Project at K.ingsport, Tennessee, is a $213.7 mil...
The project involves the construction of an 80,000 gallons per day (260 TPD) methanol unit utilizing...
The Liquid Phase Methanol (LPMEOH{trademark}) demonstration project at Kingsport, Tennessee, is a $2...
The commercial reactor type proposed for the liquid phase methanol synthesis (LPMeOH™) process is a ...