Abstract: A high rate reactor for the treatment of biosludge has been designed which combines the processes of landfarming, sand bed dewatering, and forced aeration composting. The reactor is essentially a sand bed overlying a drainage system housed in an inflatable, pressurized building.The high rate reactor can effectively treat biosludge through dewatering and biodegradation. Volume reduction, stabilization, and solidification are achieved at improved rates over conventional practices. The reactor operates independent of climate and is a closed system minimizing environmental monitoring.

Abstract: A rough cut catalyst/vapor separator for fluid catalyst cracking risers which is located at the outlet of a riser and causes the oil-catalyst mixture to undergo a tight, 180 degree downward turn. The centrifugal separator is equivalent to one-half a turn inside a cyclone and causes most of the catalyst to move to the wall. Most of the oil vapors are squeezed out away from the wall. At the end of the separator is a shave-off scoop positioned to divide a predominantly catalyst phase from a predominantly oil phase. The shave-off scoops conduct the catalyst phase away from the center of the vessel and deposit it near the vessel wall where its downward flow is continued under the action of gravity. The oil vapor phase continue its downward flow for a while but then must undergo a 180 degree turn and flow upward to exit the vessel through a series of conventional cyclone separators. The second 180 degree turn of the oil vapors help separate catalyst which is not caught by the shave-off scoop.

Abstract: Provided is a novel thioether diester synthetic lubricating oil composition represented by the formula: ##STR1## in which R and R.sub.1 each represent alkyl radicals having from 1 to 6 carbon atoms, with the total number of carbon atoms in R, R, R.sub.1, and R.sub.1 ranging from about 6 to 20, and n is an integer from 2 to 5.

Abstract: An improved method for preparing amino polyols is disclosed. The method is the Mannich condensation of phenol, formaldehyde and diethanolamine in a molar ratio of (1:1:1), and then alkoxylation with a mixture of ethylene oxide and propylene oxide in a weight ratio of about 5:95 to 20:80 to form an amino polyol of hydroxyl number 440 to 515.The method gives higher yields of aromatic amino polyols of lower viscosity than those of the comparative example.

Abstract: A support assembly for the air distributor in the catalyst regenerator vessel of a fluid catalytic cracking apparatus is revealed. The support assembly comprises a primary support which fixedly connects the air distributor to the catalyst regenerator and a plurality of secondary rigid supports. The secondary rigid supports connect to both the air distributor and catalyst regenerator vessel with ball and socket joints.The support assembly allows for unrestricted multi directional thermal expansion of the air distributor without causing twisting or warping.

Abstract: The preparation of isocyanurate foams from a recycled polyethylene terephthalate polyol modified with a polyethoxylated nonylphenol is disclosed. These modified foams exhibit improved fluorocarbon solubility. The foams may be used for building roofing and sheathing applications.

Abstract: The preparation of isocyanurate foams from a recycled polyethylene terephthalate polyol modified with aromatic amino polyols, sucrose polyols, ethoxylated alphamethyl glucosides, alkoxylated glycerine or alkoxylated sorbitol is disclosed. These modified foams exhibit improved fluorocarbon solubility. The foams may be used for building roofing and sheathing applications.

Abstract: A control system has been invented for feeding settled sludge to two filter presses without the use of a surge tank. The system provides for constant feed rates from a solids settling tank, even as filter press capacity decays and the filter press is taken off stream for dumping. This is accomplished by providing two modes of operation. The first mode provides for the feeding of a single filter press. The second mode provides control when both filter presses are fed. The second mode is actuated by elevated pressure differential across a filter press, which signals the valve to move, to bring a second filter press on line while compensating for flow rate and finally shuts down the first filter press after a timed interval.The need for a surge drum is eliminated by maintaining continuous upstream and downstream operation of the filter presses in a sludge dewatering process.

Abstract: The invention is a corrosion inhibiting water-based machining fluid comprising a synergistic combination of a 2-heptyl-1-ethoxypriopionic acid imidazoline, sodium salt; free amine and a mixture of an amine salt of C.sub.8 to C.sub.14 dicarboxylic acids.

Abstract: 4,4,6-trimethylhexahydropyrimidine is partially reacted with a polyepoxide to form a room temperature Stable "B" stage epoxy resin system. This system may be stored at or near 25.degree. C. for long periods of time without further reaction. Heating of the partially cured material rapidly transforms the B-Stage product into a cross-linked material which is both temperature and chemically resistant.These properties make the product useful as preimpregnates with laminae such as cloth, paper, glass cloth and the like and for filament windings.

Abstract: A mixture of hydrocarbons consisting of gas oil and residual oil is catalytically cracked in the presence of a fluidized zeolite catalyst. The mixture of hydrocarbons is classified by boiling range as a 550.degree.-1000.degree. F. gas oil and a 1000+.degree. F. vacuum residuum. The gas oil is selectively cracked using a freshly regenerated fluid zeolite catalyst having less than 0.1 wt % residual carbon to give a high yield of desirable liquid hydrocarbon boiling from about 60.degree.-670.degree. F. The vacuum residuum is injected into the riser reactor at a point near the riser outlet to quench the cracking reactions in the gas oil. The vacuum residuum undergoes a small amount of reaction removing undesirable materials and yielding a liquid hydrocarbon boiling up to about 1000.degree. F. The amount of vacuum residuum cracking and overall yield of liquid hydrocarbons are controlled by downstream injection of vacuum residuum into the riser.

Abstract: A method for the separation of bis-(2-aminoethyl)ether from N-(2-methoxyethyl)morpholine via azeotropic distillation using an entrainer such as monoethanolamine is described. The N-(2-methoxyethyl)morpholine is selectively removed by the monoethanolamine. The N-(2-methoxyethyl)morpholine is then separated from the monoethanolamine by liquid-liquid extraction using a non polar hydrocarbon or aromatic extraction solvent and distillation.The N-(2-methoxyethyl)morpholine-monoethanolamine stream previously had no economic use. The separation is now economically effected and the N-(2-methoxyethyl)morpholine used as a polyurethane catalyst.

Abstract: Polyether polyols are modified by reaction with alkylene oxides and amino alcohol-epoxy resin adducts. The adducts are the reaction product of an epoxy resin and amino alcohol of the formula: ##STR1## wherein: x ranges from 1 to 4,y ranges from 1 to 40, andR is an alkyl of from 1 to 4 carbon atoms.These polyether polyols are used to prepare flexible polyurethane foams.

Abstract: Water soluble thickeners made by alkoxylating monohydric alcohol hydrophobes are described. The monohydric alcohol should have at least 18 carbon atoms to be properly hydrophobic. In addition, a large proportion of ethylene oxide must be added, such that the molar ratio of ethylene oxide to monohydric alcohol hydrophobe is at least 40:1. Improved results are obtained if 8-15 moles of propylene oxide are added as a block to the single mole of hydrophobe first. The alkoxylations are necessary to provide the desired viscosities and hydrophilic nature. These thickeners are particularly useful in the glycol-water based fluids of this invention.

Abstract: An improved air distribution apparatus for a regenerator in a fluid catalytic cracking process has been invented. The improvement is in the nozzles which eject air from an air ring to a bed of coke deactivated catalyst. The nozzles are positioned to take air from the centerline of the air ring and are of length 4 to 8 diameters. The nozzles are noted for reduced aspirated catalyst erosion.

Abstract: A corrosion inhibited antifreeze composition incorporating a corrosion inhibitor is described. Six dibasic salts of dicyclopentadiene dicarboxylic acid and optionally a triazole comprise the corrosion inhibitor.

Abstract: A corrosion inhibited antifreeze composition using a three-part corrosion inhibitor mixture is described. A dicarboxylic acid component, an alkali metal silicate and a triazole comprise the three corrosion inhibitors. Use of this type of mixture permits the express exclusion of amines, nitrites, nitrates, chromates, borates and phosphates and their attendant disadvantages. Nevertheless, the inventive system provides excellent corrosion resistance in alcohol-based antifreeze, particularly with respect to aluminum.

Abstract: Non-silicate, non-gelling corrosion inhibited antifreeze compositions containing a water-soluble liquid alcohol freezing point depressant and an inhibitor combination comprising an alkali metal salt of benzoic acid, an alkali metal salt of a dicarboxylic acid and an alkali metal nitrate are described. These formulations work just as well or better than silicate-based formulations in all regards and have the advantage of not having to contain expensive organo silane gellation inhibitors as do silicate-containing antifreezes. The dicarboxylic acid used preferably has eight to twelve carbon atoms.

Abstract: A corrosion inhibited antifreeze composition incorporating a corrosion inhibitor is described. The dibasic salt of naphthalene dicarboxylic acid and optionally a triazole comprise the corrosion inhibitor.

Abstract: A high temperature multipurpose grease is prepared from the lithium soap of a C.sub.12 to C.sub.24 hydroxy fatty acid, (e.g. 12-hydroxy stearic acid) and a dilithium soap of a C.sub.4 to C.sub.12 dicarboxylic acid, (e.g. dilithium azelate) wherein the acid mole ratios range from 3:1 to 0.5:1 respectively under carefully controlled processing conditions including controlled alkali addition and one step heating.