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Rice, production volume

Uses Pure azinphos-methyl is a white crystalline solid technical azinphos-methyl is a brown waxy solid. Based on toxicity, the USEPA has grouped it under RUP. Azinphos-methyl is a highly persistent, broad-spectrum insecticide. It is used for the control of mites and ticks, and it is poisonous to snails and slugs. It also is used in the control of many insect pests on a wide variety of fruit, vegetable, nut, and held crops, as well as on ornamentals, tobacco, and forest and shade trees. Outside the United States, azinphos-methyl is used in lowland rice production. Azinphos-methyl is available in emulsihable liquid, liquid flowable, ultra-low volume (ULV) liquid, and wettable powder formulations.28,29... [Pg.130]

Up until 1986 the major use for 2-j -butylphenol was in the production of the herbicide, 2-j -butyl-4,6-dinitrophenol [88-85-7] which was used as a pre- and postemergent herbicide and as a defoHant for potatoes (30). The EPA banned its use in October 1986 based on a European study which showed that workers who came in contact with 2-j -butyl-4,6-dinitrophenol experienced an abnormally high rate of reproduction problems. Erance and the Netherlands followed with a ban in 1991. A significant volume of 2-j -butyl-4,6-dinitrophenol is used worldwide as a polymerization inhibitor in the production of styrene where it is added to the reboiler of the styrene distillation tower to prevent the formation of polystyrene (31). OSBP is used in the Par East as the carbamate derivative, 2-j -butylphenyl-Ai-methylcarbamate [3766-81-2] (BPMC) (32). BPMC is an insecticide used against leaf hoppers which affect the rice fields. [Pg.66]

Fig. 4. Typical time course of fumaric acid production in fermentor by Rhizopus sp. The culture conditions were as follows 2.5-L jar fermentor containinga 1-L working volume at 35°C, 200 rpm, 1 vvm, pH 4.5 adjusted with 5 N Na2CC>3 50 g/L of glucose 5 g/L of rice bran 1 g/L of KH2P04 0.5 g/L of MgS04-7H20. Fig. 4. Typical time course of fumaric acid production in fermentor by Rhizopus sp. The culture conditions were as follows 2.5-L jar fermentor containinga 1-L working volume at 35°C, 200 rpm, 1 vvm, pH 4.5 adjusted with 5 N Na2CC>3 50 g/L of glucose 5 g/L of rice bran 1 g/L of KH2P04 0.5 g/L of MgS04-7H20.
Historically, pricing had been the biggest barrier to biodegradable polymer market development. However, growing volumes of production and the development of new technology should further allow bio-based resin makers to reduce costs. Using materials such as corn stover, wheat straw and rice straw, which remain in fields after crops are harvested, as resin feedstock, could also increase productivity and economic performance. [Pg.38]

When rain forests are cut down, for example, and converted to fields of rice or corn, the nutrient recycling mechanisms are destroyed, and as a result, the productivity of the field quickly declines. A much better approach would be to devise a production system whereby the nutrient recycling mechanisms are left intact. Extractive reserves for Brazil nuts and rubber are examples of management approaches that are compatible with sustainability of harvest (Brown et al. this volume). The trees are not destroyed when the nuts and the rubber are harvested, and consequently, the nutrient recycling mechanisms of the forest remain intact. A problem with extractive reserves however, is... [Pg.162]

Coals can produce large reservoirs of natural gas with commercial potential. In the USA alone, coal-bed gas resources are estimated to be 400 trillion cubic feet (Tcf) (1 cf= 0.0283 m ) 90 Tcf are considered to be recoverable (ICF Resources, 1990). 399 Tcf of natural gas from other conventional sources are considered recoverable (Rice, 1993). Most coals of sufficient rank have generated large volumes of gas that may be trapped by adsorption. Gas production... [Pg.3668]

Figure 5. Simulated particle volume concentration distributions in the epilimnion of Lake Zurich, assuming a net particle production flux of 8.2 cm3 m-2 day 1 and an areal hydraulic loading for the lake of 10 4cms J. For no coagulation and sedimentation, a(i,y)s,Cxp = 0 and pp = pw for sedimentation only, a(i, j)s,exp = 0 and pp = 1.05 g cm 3 for coagulation and sedimentation, >. y)s, p = 0-1 and Pp — 1-05 gcm-3. Other assumptions stated in the text. Simulations performed by M. Wiesner of Rice University, Houston, TX. Figure 5. Simulated particle volume concentration distributions in the epilimnion of Lake Zurich, assuming a net particle production flux of 8.2 cm3 m-2 day 1 and an areal hydraulic loading for the lake of 10 4cms J. For no coagulation and sedimentation, a(i,y)s,Cxp = 0 and pp = pw for sedimentation only, a(i, j)s,exp = 0 and pp = 1.05 g cm 3 for coagulation and sedimentation, >. y)s, p = 0-1 and Pp — 1-05 gcm-3. Other assumptions stated in the text. Simulations performed by M. Wiesner of Rice University, Houston, TX.

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