Big Chemical Encyclopedia

Chemical substances, components, reactions, process design ...

Articles Figures Tables About

Tank heating coils

Tank heating coil. .. 4 — 2 6 Organic—tray-by-tray 40 (12) 64 104 (12)... [Pg.38]

Stuhlbarg, D., How to Design Tank Heating Coils, Petroleum Refiner, April 1959. [Pg.364]

Shipment, Stora.ge, ndPrice. Butenediol is available in unlined steel tank cars, tank trailers, and various sized dmms. Because of its relatively high freezing point, tank cars are fitted with heating coils. The 1991 U.S. bulk price of technical grade butenediol was about 5.36 /kg. [Pg.107]

For commodities that soHdify at temperatures commonly encountered during shipping, tank cars are equipped with internal or external heating coils. In some cases, cars are insulated with both sides of the insulation protected by thin steel shells. Approximately 15% of the tank cars in the United States are constmcted for the transportation of pressuri2ed commodities, such as anhydrous ammonia and propane. [Pg.511]

Shipment and Storage. 2-Pyrrohdinone is available in steel dmms and in aluminum or stainless-steel tank cars and tank trailers. Because of its high freezing point, bulk shipments are in tanks with heating coils. Heating with hot water rather than steam avoids product discoloration. Steel (qv), stainless steel, and aluminum are satisfactory materials for storage containers. Because 2-pyrrohdinone is hygroscopic, it must be protected from atmospheric moisture. [Pg.361]

Pitch. Pitch used to be stored in solid form at the tar distillery in open bays, from which it was removed by small explosive charges. Loading of the lump pitch by mechanical shovel created a dust ha2ard both at the tar installation and at the customer s, where the lumps had to be ground before use. In the 1990s, pitch is stored in tanks heated by superheated steam or circulating hot-oil coils and transported in fiquid form in insulated rad, road tankers, or ships. When transport as a hot fiquid is not feasible, not acceptable by the customer, or for small amounts, the pitch is converted into a dust-free particulate form, ie, short rods termed pencils, pastilles, or flakes. [Pg.344]

Shipment and Storage, Specifications. A/-Vinyl-2-pyrrohdinone is available in tank cars and tank trailers and in dmms of various sizes. Shipping containers are normally steel or stainless steel. Tank cars are provided with heating coils to facihtate unloading in cold weather. Rubber, epoxy, and epoxy—phenohc coatings are attacked and must be avoided. Carbon steel has been successfully used for storage tanks, but stainless steel preserves product quahty better. Aluminum and certain phenohc coatings are also satisfactory. [Pg.523]

Siace dimer acids, monomer acids, and trimer acids are unsaturated, they are susceptible to oxidative and thermal attack, and under certain conditions they are slightly corrosive to metals. Special precautions are necessary, therefore, to prevent product color development and equipment deterioration. Type 304 stainless steel is recommended for storage tanks for dimer acids. Eor heating coils and for agitators 316 stainless steel is preferred (heating coils with about 4s m (50 ft ) of heat transfer surface ia the form of a 5.1 cm schedule-10 U-bend scroU are recommended for a 37. 9-m (10,000-gal) tank. Dimer acid storage tanks should have an iaert gas blanket. [Pg.115]

Table 5-8 gives the order of magnitude for coil-in-tank heat transfer. [Pg.331]

Steam and hot-water coils should be constructed of seamless steel tube and preferably be without joints within the tank. These coils can be either plain or finned tube. However, due to their greater surface area, finned tubes generally have a higher rate of heat transfer than plain tubes. On the basis of cost per unit surface area, finned tubes are less expensive than conventional tubes. There is also an advantage of weight saving, and complete coverage of the base area is not necessarily required to achieve specified temperatures. [Pg.253]

There are many process contaminants that may be inadvertently carried back with the condensate following either the purposeful injection of live steam into, say, an industrial manufacturing process or that can infiltrate the system due to a leaking heating coil, an open surge tank, or similar access point. [Pg.299]

An open cylindrical tank 500 mm diameter and I m deep is three quarters filled with a liquid ol density 980 kg/mJ and of specific heat capacity 3 kj/kg K. If the heat transfer coefficient from the cylindrical walls and the base of the tank is 10 W/m2 K and front the surface is 20 W/m3 K, what area of heating coil, fed with steam at 383 K. is required to heat the contents from 288 K to 368 K in a half hour The overall heat transfer coefficient for the coil may be taken as 100 W/m2 K, the surroundings we at 288 K and the heal capacity of the tank itself may be neglected. [Pg.850]

Ethanoiamine is used to absorb carbon dioxide. A tank that contained the absorption product combusted spontaneously in air, probably because of an unknown impurity and because an amine evaporation had stripped a heating coil of this compound. The fire went out later due to the carbon dioxide release caused by the compound s temperature rise. [Pg.291]

Figure 1.21. Continuous stirred tank heated by internal steam coil. Figure 1.21. Continuous stirred tank heated by internal steam coil.
Liquid flows continuously into an initially empty tank, containing a full-depth heating coil. As the tank fills, an increasing proportion of the coil is covered by liquid. Once the tank is full, the liquid starts to overflow, but heating is maintained. A total mass balance is required to model the changing liquid volume and this is combined with a dynamic heat balance equation. [Pg.43]

With the stirred-tank heater, we know quite well by now that we want to manipulate the heating coil temperature to control the tank temperature. The process function Gp is defined based on this decision. In this simple illustration, the inlet temperature is the only disturbance, and the load function is defined accordingly. From Section 2.8.2 and Eq. (2-49b) on page 2-25, we have the first order process model ... [Pg.91]

When we developed the model for the stirred tank heater, we ignored the dynamics of the heating coil. Provide a slightly more realistic model which takes into consideration the flow rate of condensing steam. [Pg.103]


See other pages where Tank heating coils is mentioned: [Pg.673]    [Pg.38]    [Pg.244]    [Pg.706]    [Pg.673]    [Pg.38]    [Pg.244]    [Pg.706]    [Pg.69]    [Pg.515]    [Pg.515]    [Pg.435]    [Pg.290]    [Pg.365]    [Pg.196]    [Pg.374]    [Pg.289]    [Pg.433]    [Pg.46]    [Pg.146]    [Pg.1050]    [Pg.2451]    [Pg.639]    [Pg.111]    [Pg.21]    [Pg.234]    [Pg.540]    [Pg.60]    [Pg.116]    [Pg.253]    [Pg.274]    [Pg.204]    [Pg.310]    [Pg.34]   
See also in sourсe #XX -- [ Pg.581 , Pg.582 ]




SEARCH



Heated tanks

Heating coils

Tank Coils

© 2024 chempedia.info