Establishing Operational Requirements

SCAQMD Rule 1141.1 Establish operating requirements for coatings and inks manufacturing. 

Total reflux exists in a distillation column, whether a binary or multicomponent system, when all the overhead vapor from the top tray or stage is condensed and returned to the top tray. Usually a column is brought to equilibrium at total reflux for test or for a temporary plant condition which requires discontinuing feed. Rather than shut down, drain and then re-establish operating conditions later, it is usually more convenient and requires less... 

In establishing specifications, the first important items to identify from the plant process material balance are normal, maximum, and minimum intake or suction flow rates together with corresponding conditions of temperature and pressure. The required discharge pressure must be established. If it is necessary or important to be able to operate at reduced or over-normal flow rates, these should be identified for the manufacturer, together with the length of time of such expected condition e.g., full time at one-half rate, 20 minutes out of every hour at 10% over normal, etc. These operating requirements may separate the types of equipment. Because it is uneconomical to purchase horsepower that cannot be used by the fluid system, ask that the manufacturer state the maximum load and/or conditions that will fully load the available horsepower of the compressor-driver unit. 

Recourse to the maintenance and repair records or a visual aid enables the engineer to establish if the planned maintenance tasks that are not to be carried out had been maintained either during the previous scheduled visit or, when next due, a planned maintenance visit. If not carried out as programmed, the engineer must ensure that the period over which no planned maintenance is proposed does not exceed any known maintenance/operational requirement. 

Sampling and analyzing the waste and exhaust emissions to verify that the operating requirements established in the permit achieve the performance standards. 

An owner/operator wishing to operate a new hazardous waste BIF is required to obtain an RCRA permit before beginning construction of the unit. The purpose of this permit is to allow the new BIF to establish operating conditions that will ensure adequate protection of human health and the environment. The BIF permit process consists of four operational phases pretrial burn, trial burn, posttrial burn, and final operating conditions. 

The remainder of this text attempts to establish a rational framework within which many of these questions can be attacked. We will see that there is often considerable freedom of choice available in terms of the type of reactor and reaction conditions that will accomplish a given task. The development of an optimum processing scheme or even of an optimum reactor configuration and mode of operation requires a number of complex calculations that often involve iterative numerical calculations. Consequently machine computation is used extensively in industrial situations to simplify the optimization task. Nonetheless, we have deliberately chosen to present the concepts used in reactor design calculations in a framework that insofar as possible permits analytical solutions in order to divorce the basic concepts from the mass of detail associated with machine computation. 

The gap between the process risk and the owner/operator s risk criteria establishes the requirements for risk reduction. The risk gap can be managed by a single safety function or by multiple functions allocated to protection layers. The team defines the risk reduction that must be provided by each safety function and allocates the safety function to a protection layer that is designed and managed to achieve the allocated risk reduction. 

The owner shall have overall responsibility for compliance with this Code and for establishing the requirements for design, construction, examination, inspection, testing, operation, and maintenance of the hydrogen piping or pipeline system. 

Oxo plants employ mixtures of highly toxic, flammable gases under pressure at high temperatures and require strict adherence to established operating safety codes and emergency reporting procedures to local, state, and federal authorities. I11 the United States, carbon monoxide is classified as both an acute, fire, and sudden release hazard. 

A direct-contact gas cooler system operates as follows Approximately 35,000 lb/hr of bone-dry air is passed over hot trays. The air is heated from 150°F to 325°F as it passes over the trays. It exits from the unit with a due point of 105°F. The hot air is sent to a direct-contact cooler, where its temperature is reduced back to 150°F. During the cooling stage, the air is dehumidified with water that is heated frpm 75°F to 105°F. The unit is rated at 3.5 inches of water pressure drop (a) Determine the number of diffusion units needed for this operation and (b) Establish the required dimensions for the direct-contact cooling tower (Hint Use standard low-pressure-drop data from the literature. Some of the older literature give pressure drop data for simple fill. See Sherwood, T. K. and C. E. Reed [6]. 

Two major barriers to the commercialization of PEM fuel cells are high cost and poor durability. The US Department of Energy has established the durability target of electrolyte membranes for automotive fuel cells at 5,000 h and for stationary fuel cells at 40,000 h with additional cost constraints and operation requirements. In commercial applications, the integrity of fuel cell membranes must... 

Since global specialty chemicals companies already operate sites in most relevant countries, average personnel costs per full-time employee can be established relatively easily. However, location-specific adjustments of the number of operators required to run a production line/plant are required. Firstly, different degrees of automation are usually deployed in developed and developing countries. This aspect is to some extent included in the plant type definition via personnel requirements that depend on the degree of automation. However, even for technically identical plants the number of operators required per shift usually differs between developed and less developed countries due to different levels of personnel productivity. Secondly, annual working hours and consequently the relationship between... 

The California market incentives helped wind and CSP developers and investors move their technologies forward, reducing cost and acquiring valuable operational experience that improved reliability. Wind engineers developed their qualifications standards during this same period like early PV technologies, wind systems often suffered from poor reliability until their certification standards were established and required in the marketplace. 

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