A weekly publication, the Texas Register serves as the journal of state agency rulemaking for Texas. Information published in the Texas Register includes proposed, adopted, withdrawn and emergency rule actions, notices of state agency review of agency rules, governor's appointments, attorney general opinions, and miscellaneous documents such as requests for proposals. After adoption, these rulemaking actions are codified into the Texas Administrative Code.

The CO conversion and isobutylene yield for Runs 11 to 20 (except run 12) at the conditions of 450[degree]C, 1,200 psig, and 1,920 gas hourly space velocity (GHSV), Is given in Table 2. These conditions generally provide the maximum CO conversion for each run. Runs 5 to 10 is also provided in Table 2 for a comparison. The description of the catalysts also given in Table 2 includes the composition, method of preparation, and calcination temperature for each catalyst tested. Data for Runs 12 and 21 are at different conditions, as discussed later in this report. The conversion and yield data were obtained at relatively short times on-stream ([approximately]11 hours). The extent of catalyst deactivation has not been determined. The freshly precipitated CeO[sub 2] catalyst, IS-9, is by far the most active but is poorly selective to Isobutene. The catalyst primarily produces saturated by-products. The commercial CeO[sub 2,] IS-8, had low surface area and little activity. Earlier tests show that lowering the calcination temperature of precipitated catalysts produced higher surface areas, higher tetragonal content, higher activity and higher yields. The ZrO[sub 2] sol-gel catalysts show a similar relationship. A comparison of Run 9 (ZrO[sub 2] calcined at 600[degree]C) and Run …

The CO conversion and isobutylene yield for Runs 11 to 20 (except run 12) at the conditions of 450{degree}C, 1,200 psig, and 1,920 gas hourly space velocity (GHSV), Is given in Table 2. These conditions generally provide the maximum CO conversion for each run. Runs 5 to 10 is also provided in Table 2 for a comparison. The description of the catalysts also given in Table 2 includes the composition, method of preparation, and calcination temperature for each catalyst tested. Data for Runs 12 and 21 are at different conditions, as discussed later in this report. The conversion and yield data were obtained at relatively short times on-stream ({approximately}11 hours). The extent of catalyst deactivation has not been determined. The freshly precipitated CeO{sub 2} catalyst, IS-9, is by far the most active but is poorly selective to Isobutene. The catalyst primarily produces saturated by-products. The commercial CeO{sub 2,} IS-8, had low surface area and little activity. Earlier tests show that lowering the calcination temperature of precipitated catalysts produced higher surface areas, higher tetragonal content, higher activity and higher yields. The ZrO{sub 2} sol-gel catalysts show a similar relationship. A comparison of Run 9 (ZrO{sub 2} calcined at 600{degree}C) and Run …

Weekly newsletter discussing natural resources, parks, hunting and fishing, and other information related to the outdoors in Texas.

This report describes the CTCN computer code, designed to solve the equations of transient colloidal transport of radionuclides in porous and fractured media. This Fortran 77 package solves systems of coupled nonlinear differential equations with a wide range of boundary conditions. The package uses the Method of Lines technique with a special section which forms finite-difference discretizations in up to four spatial dimensions to automatically convert the system into a set of ordinary differential equations. The CTCN code then solves these equations using a robust, efficient ODE solver. Thus CTCN can be used to solve population balance equations along with the usual transport equations to model colloid transport processes or as a general problem solver to treat up to four-dimensional differential systems.