Environmentally acceptable process for disposing of scrap plastic materials

Abstract: A pumpable slurry of shredded scrap solid carbonaceous plastic-containing material that contains associated inorganic matter in admixture with a comminuted aluminosilicate-containing material having noncombustible constituents is reacted by partial oxidation to produce synthesis gas, reducing gas, or fuel gas. The noncombustible constituents in the aluminosilicate-containing material captures the inorganic matter in the scrap solid carbonaceous plastic-containing material while in the reducing atmosphere of the gasifier to produce nontoxic, nonleachable slag. The slurrying medium is water, liquid hydrocarbonaceous fuel, or mixtures thereof. Scrap plastics may be disposed of by the subject process without polluting the nation's environment.

Description: FIELD OF THE INVENTION This invention relates to an environmentally safe method for disposing of scrap plastic materials. More particularly, it pertains to a process for the partial oxidation of a pumpable slurry of shredded scrap solid carbonaceous plastic-containing material that contains associated inorganic matter in admixture with a comminuted aluminosilicate-containing material having noncombustible constituents. The liquid slurrying medium may be water and/or liquid hydrocarbonaceous fuel. The inorganic matter in the solid carbonaceous plastic-containing material is safely captured by the noncombustible constituents in the aluminosilicate-containing material to produce nonhazardous slag. Scrap plastics are solid organic polymers and are available in such forms as sheets, extruded shapes, moldings, reinforced plastics, laminates, and foamed plastics. About 60 billion pounds of plastics are sold in the United States each year. A large part of these plastic materials wind up as scrap plastics in landfills. Although plastics account for only a small portion of the waste dumped in landfills i.e. about 7 wt. % and about 20 percent by volume, burying them is getting increasingly difficult. Landfills are not universally viewed as an acceptable, or even a tolerable option for disposal of plastic materials. Due to the combined effects of the unpopularity of existing facilities and the need for land to allow normal growth of populations, new landfills have been all but banned in many parts of the world. Existing facilities are also facing finite limits as to how long they may continue to function. Also, toxic wastes from buried plastics seep into and pollute underground streams which are commonly the source of our fresh water. Further, on-site burning or incineration which are alternative disposal methods are in disfavor because they generate heavy air pollution from noxious gases and soot. With respect to recycling plastics, it has been economically feasible to recycle only about 1 wt. % of the scrap plastics. It is obvious from the aforesaid that the disposal of scrap plastics is one of the nation's most pressing environmental problems. SUMMARY OF THE INVENTION This invention provides a process for disposing of scrap plastic materials in accordance with claim 1. DESCRIPTION OF THE INVENTION Scrap plastics are disposed of by the process of the subject invention without polluting the nation's environment. In one embodiment, troublesome coal ash resulting from the complete combustion of coal in a power plant is simultaneously disposed of by means of the subject environmentally acceptable process. Simultaneously, useful by-product nonpolluting synthesis gas, reducing gas, fuel gas and nonhazardous slag are produced. In addition, profitable by-product steam and hot water for use in the process or export are produced. The scrap plastic materials which are used as feed in the subject process as fuel to a partial oxidation gas generator include at least one solid carbonaceous thermoplastic or thermosetting material that contains associated inorganic matter. Sulfur is also commonly found in scrap plastics. Scrap plastic materials may be derived from obsolete equipment, household containers, packaging, industrial sources and junked automobiles. The mixture of plastics is of varying age and composition. With the presence of varying amounts of incombustible inorganic matter compounded in the plastic as fillers, catalysts, pigments and reinforcing agents, recovery of the plastic material is generally impractical. Further, complete combustion can release toxic-noxious components including volatile metals and hydrogen halides. Associated inorganic matter in the scrap solid carbonaceous plastic includes fillers such as titania, talc, clays, alumina, barium sulfate and barium carbonate. Catalysts and accelerators for thermosetting plastics include tin compounds for polyurethanes, and cobalt and manganese compounds for polyesters. Dyes and pigments such as compounds of cadmium, chromium, cobalt, and copper; non-ferrous metals such as aluminum and copper in plastic coated wire cuttings; metal films; woven and nonwoven glass and boron reinforcing agents; steel, brass, and nickel metal inserts; and lead compounds from plastic automotive batteries. The inorganic constituents are present in the solid carbonaceous plastic-containing material in the amount of about a trace amount to about 80 wt. % of said solid carbonaceous plastic-containing material, such as about 0.1 to 60 wt. %, say about 1 to 20 wt. % of the plastic-containing material. The scrap plastic material is in the form of sheets, extruded shapes, moldings, reinforced plastics, and foamed plastics. In the subject process, a pumpable slurry is prepared having a total solids content in the range of about 10 to 70 wt. % when the slurrying medium comprises a liquid hydrocarbonaceous fuel; about 30 to 70 wt. % when the slurrying medium comprises water; and about 25 to 70 wt. % when the slurrying medium comprises a mixture of water and liquid hydrocarbonaceous fuel. The solids in the pumpable slurry includes solid carbonaceous plastic-containing material that contains associated inorganic matter and aluminosilicate-containing material having noncombustible constituents. A minimum of 5 wt. % of the total solids in the pumpable slurry is solid carbonaceous plastic-containing material that contains associated inorganic matter. The remainder of the solids in the pumpable slurry substantially comprises said aluminosilicate-containing material having noncombustible constituents. The pumpable slurry is introduced into a partial oxidation gas generator where reaction takes place, with or without, a supplemental temperature moderator. By definition, the term liquid hydrocarbonaceous fuel as used herein to describe suitable liquid carriers and fuels is selected from the group consisting of liquefied petroleum gas, petroleum distillates and residues, gasoline, naphtha, kerosine, crude petroleum, asphalt, gas oil, residual oil, tar sand oil and shale oil, coal derived oil, aromatic hydrocarbons (such as benzene, toluene, xylene fractions), coal tar, cycle gas oil from fluid-catalytic-cracking operation, furfural extract of coker gas oil, oxygen-containing liquid hydrocarbonaceous organic materials including cellulosic materials and alcohols, and mixtures thereof. Waste motor oil may also be used as a liquid carrier. In one embodiment, a pumpable slurry having two categories of solid carbonaceous plastic material and a solids content in the range of about 25 to 70 wt. % is fed to the partial oxidation gas generator. About 10 to 95 wt. %, such as about 25 to 75 wt. % of the solid carbonaceous plastic material comprises solid carbonaceous plastic-containing material that contains associated inorganic matter. The remainder of the solid carbonaceous plastic materials comprising about 90 to 5 wt. %, such as about 75 to 25 wt. % of the total solid carbonaceous plastic-containing material comprises solid carbonaceous plastic material that is substantially free from associated inorganic matter. The term "substantially free" means that the inorganic matter is less than 0.01 wt. % of the solid carbonaceous plastic-containing material. The expression "A and/or B" is used herein in its usual manner and means A or B or A and B. Figure 1 gives a breakdown of 1991 sales in the United States of solid carbonaceous plastics. Million lbs. Material 1991 Acrylobutadienestyrene (ABS) 1,125 Acrylic 672 Alkyd 315 Cellulosic 840 Epoxy 428 Nylon 536 Phenolic 2,556 Polyacetal 140 Polycarbonate 601 Polyester, thermoplastic 2,549 Polyester, unsaturated 1,081 Polyethylene, high density 9,193 Polyethylene, low density 12,143 Polyphenylene-based alloys 195 Polypropylene and copolymers 8,155 Polystyrene 4,877 Other styrenes 1,180 Polyurethane 2,985 Polyvinylchloride and copolymers 9,130 Other vinyls 120 Styrene acrylonitrile (SAN) 117 Thermoplastic elastomers 584 Urea and melamine 1,467 Others 345 Total 60,598 The aluminosilicate-containing material that is used as a feedstream in the process is a nonpolymeric material selected from the group of solid materials consisting of coal, associated coal residues such as mine tailings, coal ash, clay (such as illite), and volcanic ash. About 5 to 100 wt. % of the aluminosilicate-containing material comprises inorganic noncombustible constituents. This mixture of constituents has an ash fusion temperature in a reducing atmosphere, such as that in the partial oxidation gas generator, of less than about 1316°C (2400°F). Any remainder comprises carbonaceous material. Any type of coal may be used as the aluminosilicate-containing material including anthracite, bituminous, sub-bituminous, and lignite. The inorganic constituents in coal substantially comprises aluminosilicate clay materials (illite, smectite, kaolinite), sulfides (pyrite, pyrrhotite), carbonates (calcite, dolomite, siderite), and oxides (quartz, magnetite, rutile, hematite). The mole ratio SiO 2 /Al 2 O 3 in the aluminosilicate-containing material is in the range of about 1.5/1 to 20/1. Further, the total moles of oxides selected from the group consisting of Na, K, Mg, Ca, Fe, and mixtures thereof is about 0.9 to 3 times the moles of Al 2 O 3 . In one embodiment, the composition of the aluminosilicate can be represented as (Na 2 O, K 2 O, MgO, CaO, FeO) x · Al 2 O 3 · (SiO 2 ) y where x is from 0.9 to 3 and y is from 1.5 to 20. The total amount of alumina, silica, and the oxides of Na, K, Mg, Ca and Fe constitutes at least 90 wt. % of the total noncombustible inorganic components. The solid carbonaceous plastic-containing material that contains associated inorganic matter has a higher heating value (HHV) in the range of about 7 to 44 MJ/kg (3000 to 19,000 BTU per lb) of solid carbonaceous plastic-containing material. The plastic-containing material is shredded by conventional means to a maximum particle dimension of about 6.3 mm (1/4"), such as about 3.2 mm (1/8"). Shredding is the preferred method for reducing the size of plastic. Grinding is less effective and more energy intensive. The aluminosilicate-containing material having noncombustible constituents that have an ash fusion temperature in a reducing atmosphere of less than about 1316°C (2400°F) has a higher heating value (HHV) in the range of about 0 to 35 MJ/kg (0 to 15,000 BTU per lb) of aluminosilicate-containing material. The aluminosilicate-containing material is ground by conventional means to a particle size so that 100% passes through ASTM E 11-70 Standard Sieve Designation 1.70 mm (Alternative No. 12). The shredded solid carbonaceous plastic-containing material and the aluminosilicate-containing material are mixed together with a liquid slurrying medium selected from the group consisting of water, liquid hydrocarbonaceous fuel, and mixtures thereof to produce a pumpable slurry having a minimum higher heating value (HHV) of about 10.5 MJ/kg (4500 BTU/lb) of slurry. The weight ratio of the noncombustible constituents in the aluminosilicate-containing material to the associated inorganic matter in said solid carbonaceous plastic-containing material is at least 1:1 and preferably at least 3:1. A suitable surfactant may be introduced into an aqueous slurry of solid carbonaceous plastic-containing material that contains associated inorganic matter and aluminosilicate-containing material having noncombustible constituents in order to increase the slurryability, pumpability, and solids content. About 0.01 to 3.0 wt. %, such as about 0.1 to 2.0 wt. % of ammonium lignosulfonate has been found to be effective. This surfactant is manufactured and marketed under the trademark of ORZAN A, by Crown Zellerbach Corp., Chemical Products Division, Vancouver, Washington. The slurry of scrap solid carbonaceous plastic-containing material and aluminosilicate-containing material and a stream of free-oxygen containing gas are introduced into the reaction zone of a free-flow unobstructed downflowing vertical refractory lined steel wall pressure vessel where the partial oxidation reaction takes place. A typical gas generator is shown and described in coassigned U.S. Pat. No. 3,544,291. A two, three or four stream annular type burner, such as shown and described in coassigned U.S. Pat. Nos. 3,847,564, and 4,525,175, may be used to introduce the feedstreams into the partial oxidation gas generator. With respect to U.S. Pat. No. 3,847,564, free-oxygen containing gas may be simultaneously passed through the central conduit 18 and outer annular passage 14 of said burner. The free-oxygen containing gas is selected from the group consisting of substantially pure oxygen i.e. greater than 95 mole % O 2 , oxygen-riched air i.e. greater than 21 mole % O 2 , and air. The free-oxygen containing gas is supplied at a temperature in the range of about 38°C to 538°C (100°F to 1000°F). The slurry of scrap solid carbonaceous plastic-containing material and aluminosilicate-containing material is passed through the intermediate annular passage 16 at a temperature in the range of about ambient to 343°C (650°F). The burner assembly is inserted downward through a top inlet port of the noncatalytic synthesis gas generator. The burner extends along the central longitudinal axis of the gas generator with the downstream end discharging a multiphase mixture of fuel, free-oxygen containing gas, and optionally a temperature moderator such as water or steam directly into the reaction zone. In the case of an aqueous slurry, the temperature moderator may be unnecessary. The relative proportions of fuels, water and oxygen in the feedstreams to the gas generator are carefully regulated to convert a substantial portion of the carbon in the slurry, e.g., up to about 90% or more by weight, to carbon oxides; and to maintain an autogenous reaction zone temperature in the range of about 982°C to 1927°C (1800°F to 3500°F). Preferably the temperature in the gasifier is in the range of about (1316°C to 1538°C (2400°F to 2800°F), so that molten slag is produced. Further, the weight ratio of H 2 O to carbon in the feed is in the range of about 0.2 to 3.0, such as about 0.5 to 2.0. The atomic ratio of free-oxygen to carbon in the feed is in the range of about 0.8 to 1.4, such as about 0.9 to 1.2. By the aforesaid operating conditions, a reducing atmosphere comprising H 2 + CO is produced in the reaction zone along with nontoxic slag. The dwell time in the reaction zone is in the range of about 1 to 15 seconds, and preferably in the range of about 2 to 8 seconds. With substantially pure oxygen feed to the gas generator, the composition of the effluent gas from the gas generator in mole % dry basis may be as follows: H 2 10 to 60, CO 20 to 60, CO 2 5 to 60, CH 4 nil to 5, H 2 S+COS nil to 5, N 2 nil to 5, and Ar nil to 1.5. With air feed to the gas generator, the composition of the generator effluent gas in mole % dry basis may be about as follows: H 2 2 to 20, CO 5 to 35, CO 2 5 to 25, CH 4 nil to 2, H 2 S+COS 0 to 3, N 2 45 to 80, and Ar 0.5 to 1.5. Unconverted carbon, ash, or molten slag are contained in the effluent gas stream. Depending on the composition and use, the effluent gas stream is called synthesis gas, reducing gas, or fuel gas. For example, synthesis gas comprises mixtures of H 2 + CO that can be used for chemical synthesis; reducing gas is rich in H 2 + CO and is used in reducing reactions; and fuel gas comprises mixtures of H 2 + CO and also includes CH 4 . Coal has an ash content of about 5 to 30 wt. %. It was unexpectedly found that advantageously when coal is used as the aluminosilicate-containing material the ash from the coal will capture the noncombustible materials in the plastic materials, and the encapsulated material will flow from the reaction zone of the gas generator as substantially inert molten slag. Advantageously, in the extremely hot reducing atmosphere of the gasifier, the toxic elements in the inorganic matter in the solid carbonaceous plastic-containing material are captured by the noncombustible constituents in the aluminosilicate-containing material and converted into nontoxic nonleachable slag. This permits the nontoxic slag to be sold as a useful by-product. For example, the cooled slag may be ground or crushed to a small particle size e.g. less than 3.2 mm (1/8") and used in road beds or building blocks. The hot gaseous effluent stream from the reaction zone of the synthesis gas generator is quickly cooled below the reaction temperature to a temperature in the range of about 121°C to 371°C (250°F to 700°F) by direct quenching in water, or by indirect heat exchange for example with water to produce steam in a gas cooler. The gas stream may be cleaned and purified by conventional methods. For example, reference is made to coassigned U.S. Pat. No. 4,052,176, for removal of H 2 S, COS, and CO 2 . Advantageously, when gasifying plastics that contain halides such as polyvinylchloride, polytetrafluoroethylene, by partial oxidation, the halide is released as hydrogen halide (i.e. HCl, HF) and is scrubbed out of the synthesis gas with water containing ammonia or other basic materials. Plastics that contain bromine-containing fire retardants may be similarly treated. Reference is made to coassigned U.S. 4,468,376. The following examples illustrate the subject invention and should not be construed as limiting the scope of the invention. EXAMPLES Example 1 3.6t (4 tons) per day of a mixture comprising several types of plastic that are found in automobiles including unfilled, filled, and reinforced plastics from the following resins: polyamide, polyurethane, polyvinylchloride, polypropylene, and others are shredded to a particle dimension of less than about 3.2 mm (1/8") and mixed with 65.7t (72.4 tons) per day of water and 66.2t (73 tons) per day of bituminous coal having an ash content of about 10 wt. % and having an ash with an ash fusion temperature in a reducing atmosphere of below 1260°C (2300°F). The coal is ground to a particle size so that 100% passes through ASTM E 11-70 Standard Sieve Designation 1.7 mm (Alternative No. 12) to produce a pumpable slurry having a maximum viscosity of 1 pa.s (1000 cp) when measured at 71°C (160°F) and a higher heating value of 20 MJ/kg (8500 BTU/lb) of slurry. The ultimate chemical analysis of a typical shredded mixture of plastics is shown in Table I. The chemical analysis of the ash in the mixture of plastics is shown in Table II. Dry Analysis of Mixture of Plastics In Example 1. Percent C 23.8 H 4.2 N 0.9 S 0.5 O 12.3 Ash 58.3 Chemical Analysis of the Ash Present In the Mixture of Plastics In Example 1. Wt. % SiO 2 33.20% Al 2 O 3 6.31% Fe 2 O 3 22.00% CaO 29.20% MgO 0.94% Na 2 O 1.27% K 2 O 0.43% TiO 2 0.89% P 2 O 3 0.92% Cr 2 O 3 0.28% ZnO 2.31% PbO 0.09% BaO 0.80% CuO 0.89% NiO 0.00% The aforesaid pumpable aqueous slurry of plastics and coal is reacted with about 68t (75 tons) per day of oxygen gas by partial oxidation in a conventional freeflow noncatalytic gas generator at a temperature of about 1316°C (2400°F) and a pressure of about 3.5 MPa (500 psig). Synthesis gas comprising H 2 + CO is produced along with about 9t (10 tons) of slag. Upon cooling, the slag is a coarse, glassy nonleachable material. If however, the same mixture of plastics were fully combusted in air, the slag may contain toxic elements, e.g. chromium in a leachable form. Example 2 45.4t (50 tons) per day of a mixture comprising several types of plastics that are found in the household including unfilled, filled, and foamed plastics, comprising polyethylene terephthalate, polyethylene, polyamide, polyurethane, polystyrene, polyvinylchloride, and polypropylene, are shredded to a particle dimension of about 3.2 mm (1/8") and mixed with 32t (35 tons) per day of residual fuel oil, and 3.6t (4 tons) per day of coal ash having an ash fusion temperature in a reducing atmosphere of about 1266°C (2310°F). The coal ash having a particle size of less than 12 mesh i.e. 1.6 mm (1/16") is obtained by filtering stack gases from a complete combustion coal-fired boiler. The composition of the coal ash is shown in Table III. A pumpable slurry is produced having a higher heating value of about 37 MJ/kg (16,000 BTU/lb) of slurry. The ultimate chemical analysis of the shredded mixture of plastics is shown in Table IV. The chemical analysis of the ash in the mixture of plastics is shown in Table V. Chemical Anslysis of Coal Ash In Example 2. Wt. % SiO 2 54.51 Al 2 O 3 14.58 Fe 2 O 3 6.37 MgO 2.80 CaO 17.36 Na 2 O 3.13 K 2 O 0.12 TiO 2 0.94 P 2 O 5 0.15 MnO 0.05 Ultimate Analysis of Shredded Mixture of Plastics In Example 2. Percent C 82.3 H 10.2 N 0.0 S 0.1 O 5.6 Ash 1.8 Chemical Analysis of the Ash Present In the Mixture of Plastics In Example 2. Wt. % SiO 2 30.63 Al 2 O 3 35.89 Fe 2 O 3 2.93 CaO 5.38 MgO 1.64 Na 2 O 4.55 K 2 O 0.82 TiO 2 16.23 P 2 O 3 0.71 Cr 2 O 3 0.00 ZnO 0.62 PbO 0.10 BaO 0.19 CuO 0.07 NiO 0.07 The aforesaid pumpable slurry of plastics, and coal ash is reacted with about 7.3t (8 tons) per day of water temperature moderator and 84t (93 tons) per day of oxygen gas by partial oxidation in a conventional free-flow noncatalytic gas generator at a temperature of about 1316°C (2400°F) and a pressure of about 3.5 MPa (500 psig). Synthesis gas comprising H 2 + CO is produced along with about 4.5t (5 tons) of nonleachable slag. The hydrogen content in the raw gas stream produced in Examples 1 and 2 may be increased by the well-known water gas shifting of the CO and H 2 O. Acid-gases e.g. CO 2 , H 2 S and COS may be removed from the raw product gas stream by conventional gas purification methods. The nontoxic nonleachable slag may be used for example as road fill. Advantageously, the toxic materials in the plastic, residual oil and coal ash, are captured in the slag in a nonleachable form and are thereby rendered nontoxic. Other modifications and variations of the invention as hereinbefore set forth may be made without departing from the scope thereof, and therefore, only such limitations should be imposed on the invention as are indicated in the appended claims.

Claims: A process for disposing of scrap plastic material comprising: (1) mixing together the following materials to produce a pumpable slurry having a minimum HHV of about 10.5 MJ/Kg (4500 BTU/lb.) of slurry: (a) solid carbonaceous plastic-containing material that contains associated inorganic matter comprising at least one material selected from the group consisting of titania, talc, clays, alumina, glass, barium sulfate, and barium carbonate; compounds of Sn, Co, Mn, Pb, Cd, Cr, Cu, B; and steel, nickel, aluminum, brass and copper metal; and wherein said solid carbonaceous plastic-containing material has a maximum particle dimension of about 6.3 mm (¼''); (b) aluminosilicate-containing material having noncombustible constituents that have an ash fusion temperature in a reducing atmosphere of less than about 1316°C (2400°F); wherein said aluminosilicate containing material is selected from the group consisting of coal, coal mine tailings, coal ash, illite clay, volcanic ash, and mixtures thereof; and wherein said aluminosilicate-containing material has: A. a maximum particle size of ASTM E11-70 Sieve Designation Standard 1.70 mm; B. a weight ratio of noncombustible constituents in said aluminosilicate-containing material to the inorganic matter in said solid carbonaceous plastic-containing material of at least 1 to 1; and C. a mole ratio SiO 2 /Al 2 O 3 in the range of about 1.5/1 to 20/1; and (c) a liquid slurrying medium selected from the group consisting of water, liquid hydrocarbonaceous fuel, and mixtures thereof; and (2) reacting said pumpable slurry from (1) with a free-oxygen containing gas and with or without a supplemental temperature moderator in a free-flow unobstructed downflowing vertical partial oxidation gas generator in a reducing atmosphere at a weight ratio of H 2 O to carbon in the feed in the range of about 0.2 to 3.0, an atomic ratio of free-oxygen to carbon in the feed in the range of about 0.8 to 1.4, and a dwell time in the range of about 1 to 15 seconds to produce synthesis gas, reducing gas, or fuel gas; and wherein said inorganic matter in said solid carbonaceous plastic-containing material in (1) (a) is safely captured by said noncombustible constituents in said aluminosilicate-containing material from (1) (b) to produce nonhazardous slag. The process according to Claim 1 wherein said solid carbonaceous plastic-containing material (1) (a) constitutes a minimum of 5 wt. percent of the total solids in said pumpable slurry. A process according to Claim 1 or Claim 2 wherein said noncombustible constituents in (1) (b) comprise the elements Al, Si and at least one element from the group consisting of Na, K, Mg, Ca and Fe. A process according to any one of Claims 1 - 3 wherein said aluminosilicate-containing material in (1) (b) has a total moles of oxides selected from the group consisting of Na, K, Mg, Ca, Fe, and mixtures thereof of about 0.9 to 3 times the moles of Al 2 O 3 ; and a total amount of Al 2 O 3 , SiO 2 , and the oxides of Na, K, Mg, Ca, and Fe that constitutes at least 90 wt. % of the total noncombustible inorganic components. A process according to any one of Claims 1 - 4 wherein the total solids content of said pumpable slurry in (1) with an aqueous slurrying medium in (1) (c) is in the range of about 30 to 70 wt. %; with a liquid hydrocarbonaceous fuel slurrying medium in (1) (c) the total solids content of said pumpable slurry in (1) is in the range of about 5 to 70 wt. %; and with a mixture of liquid hydrocarbonaceous fuel and water slurrying medium in (1) (c), the total solids content of said pumpable slurry in (1) is in the range of about 25 to 70 wt. %. A process according to any one of Claims 1 - 5 wherein said inorganic matter in (1) (a) is present in the amount of about a trace amount to 80 wt. % of the solid carbonaceous plastic-containing material; and said noncombustible constituents of the aluminosilicate-containing material in (1) (b) are present in the amount of about 5 to 100 wt. % of said aluminosilicate-containing material. A process according to any one of Claims 1 - 6 wherein about 0.1 to 60 wt. % of the solid carbonaceous plastic-containing material in (1)(a) comprises associated inorganic matter; the aluminosilicate-containing material in (1)(b) is coal; and the slurrying medium in (1)(c) comprises water with or without liquid hydrocarbonaceous fuel. A process according to any one of Claims 1 - 7 wherein said solid carbonaceous plastic-containing material is separately shredded and said aluminosilicate-containing material is separately ground. A process according to any one of Claims 1 - 8 provided with the step of introducing into said pumpable slurry in (1) a supplemental amount of a solid carbonaceous plastic-containing material that is substantially free from associated inorganic matter. A process according to Claim 9 wherein from about 10 to 95 wt. % of the solid carbonaceous plastic-containing material in the slurry comprises said solid carbonaceous plastic-containing material that contains associated inorganic matter and the remainder of the solid carbonaceous plastic-containing material in said slurry comprises solid carbonaceous plastic-containing material that is substantially free from associated inorganic matter. A process according to any one of Claims 1 - 10 wherein said pumpable slurry in (1) is an aqueous slurry and ammonium lignosulfonate is introduced into said slurry in the amount of about 0.01 to 3.0 wt. % of said slurry. A process according to any one of Claims 1 - 11 wherein said solid carbonaceous plastic-containing material in (1) (a) includes a halogen-containing plastic material and the product gas stream in (2) contains a hydrogen halide; and provided with the step of scrubbing said product gas stream with water containing ammonia or other basic material to remove said hydrogen halide. A process according to Claim 12 wherein said halogen-containing plastic material is polyvinylchloride and/or polytetrafluoroethylene and said hydrogen halide is HCl if polyvinylchloride is present and/or HF if polytetrafluoroethylene is present. A process according to Claim 1 wherein, in step (1), said pumpable slurry has a solids content in the range of about 25 to 70 wt. % and said materials (a) and (b) comprise: (a) at least one type of solid carbonaceous thermoplastic or thermosetting plastic-containing material that contains at least one inorganic ingredient in the amount of about 0.1 to 60 wt. % of said plastic-containing material; (b) bituminous coal containing inorganic ash having an ash fusion temperature in a reducing atmosphere of less than about 1316°C (2400°F) and said ash constituting about 5 to 30 wt. % of said coal; wherein the weight ratio of said ash in (b) to inorganic ingredient in (a) is at least 1; and wherein, in step (2), the pumpable slurry from (1) is introduced into said reaction zone of said free-flow unobstructed downflowing, vertical partial oxidation gas generator by way of the intermediate annular passage of a multi-passage annular burner comprising a central conduit, an intermediate coaxial annular passage, and an outer coaxial, annular passage, with a stream of free-oxygen containing gas being passed through said central conduit and outer annular passage.

Inventors: ALBERT CHRISTINE CORNELIA, CRIKELAIR DAVID CHARLES, KHAN MOTASIMUR RASHID, RICHTER GEORGE NEAL, STEVENSON JOHN SAUNDERS, ALBERT, CHRISTINE CORNELIA, CRIKELAIR, DAVID CHARLES, KHAN, MOTASIMUR RASHID, RICHTER, GEORGE NEAL, STEVENSON, JOHN SAUNDERS
Applicants: TEXACO DEVELOPMENT CORP, TEXACO DEVELOPMENT CORPORATION
Application year: 1993
Main classification: C10J3
IPC codes: B09B3, C10J3, C10L1