Abstract An apparatus for the disposal of scrap vinyl polymers containing chlorine and hydrogen. The apparatus includes a rotary kiln that is adapted to receive said scrap plastic and heat the same to a temperature at which the plastic partially decomposes, and the major portion of the chlorine escaping therefrom as hydrogen chloride gas, which gas together with any chlorine which results from the decomposition is recovered in a confined space for subsequent usage. The partially decomposed scrap plastic is sequentially removed from the rotary kiln in a dried state and crushed. The crushed plastic is discharged by a blower onto a grate in a furnace where the scrap plastic is burned. The hot gases of combustion from the burning together with fines and dust arising from the burning operation are conducted through a passage to heat air that is subsequently used in the heating of the rotary kiln. The hot gases of combustion, together with entrained solid materials, are discharged into a dust collector to remove the fines and dust therefrom. The gases after being freed of solid materials are subsequently discharged through a chimney to the ambient atmosphere. The gases discharged to the ambient atmosphere are substantially free of chlorine and hydrogen chloride gases.
An incinerator device for recovering hydrogen chloride from scrap plastic prior to the latter being burned, said plastic of a type that contains hydrogen and chlorine and that partially decomposes to yield substantially hydrogen chloride only when heated to a first temperature, said incinerator device including: a. an angularly disposed rotary, power driven kiln having first and second open ends, said first end higher than said second end, and said kiln capable of having said scrap plastic heated therein to said first temperature; b. a hydrogen chloride collecting chamber in communication with said first end; c. a hydrogen chloride collector in communication with said chamber; d. first means for sequentially discharging said scrap plastic at a desired rate into said first end of said kiln for said scrap plastic to be partially decomposed when heated to said first temperatuRe; e. second power operated means for crushing said partially decomposed plastic as the latter discharges by gravity from said second end of said kiln; f. a downwardly extending chute through which crushed partially decomposed plastic is received from said second power-operated means; g. a furnace that includes a grate onto which said crushed partially decomposed plastic is discharged from said chute; h. third means for supplying a surplus of air to the interior of said furnace as said partially decomposed plastic burns to gaseous products of combustion on said grate; i. a jacket extending around said kiln to receive a heated fluid at a temperature sufficient to heat the interior of said kiln to said first temperature, said jacket and collecting chamber obstructing communication between said first and second ends of said kiln and the ambient atmosphere; j. a heat exchanger that is heated by said gaseous products of combustion to a second temperature higher than said first temperature, said heat exchanger having a first end through which fluid can enter to be heated, and a second end through which heated fluid can discharge; k. a power driven pump having an inlet and a discharge; l. first conduit means connecting said discharge to said first end of said heat exchanger; m. second conduit means connecting said second end of said heat exchanger to the interior of said jacket for said heated fluid from said heat exchanger to heat said kiln to said first temperature; n. third conduit means connecting said inlet of said pump to the interior of said jacket to permit a continuous circulation of said heated fluid to said jacket; o. a chimney in communication with the interior of said furnace only to receive said gaseous products of combustion and discharge the same to the ambient atmosphere after said gaseous products of combustion have heated said heat exchanger; and p. fourth means for controlling the temperature of said heat exchanger to one at which said fluid is heated to the extent that said kiln is maintained at said first temperature at which substantially hydrogen chloride only is obtained from the partial decomposition of said plastic in said kiln.
Claim 2
Dependent Claim
499 words
An incinerator device for recovering hydrogen chloride from scrap plastic prior to the latter being burned, said plastic of a type that contains hydrogen and chlorine and that partially decomposes to yield substantially hydrogen chloride only when heated to a first temperature, said incinerator device including: a. an angularly disposed rotary, power driven kiln having first and second open ends, said first end higher than said second end, and said kiln capable of having said scrap plastic heated therein to said first temperature; b. a hydrogen chloride collecting chamber in communication with said first end; c. a hydrogen chloride collector in communication with said chamber; d. first means for sequentially discharging said scrap plastic at a desired rate into said first end of said kiln for said scrap plastic to be partially decomposed when heated to said first temperatuRe; e. second power operated means for crushing said partially decomposed plastic as the latter discharges by gravity from said second end of said kiln; f. a downwardly extending chute through which crushed partially decomposed plastic is received from said second power-operated means; g. a furnace that includes a grate onto which said crushed partially decomposed plastic is discharged from said chute; h. third means for supplying a surplus of air to the interior of said furnace as said partially decomposed plastic burns to gaseous products of combustion on said grate; i. a jacket extending around said kiln to receive a heated fluid at a temperature sufficient to heat the interior of said kiln to said first temperature, said jacket and collecting chamber obstructing communication between said first and second ends of said kiln and the ambient atmosphere; j. a heat exchanger that is heated by said gaseous products of combustion to a second temperature higher than said first temperature, said heat exchanger having a first end through which fluid can enter to be heated, and a second end through which heated fluid can discharge; k. a power driven pump having an inlet and a discharge; l. first conduit means connecting said discharge to said first end of said heat exchanger; m. second conduit means connecting said second end of said heat exchanger to the interior of said jacket for said heated fluid from said heat exchanger to heat said kiln to said first temperature; n. third conduit means connecting said inlet of said pump to the interior of said jacket to permit a continuous circulation of said heated fluid to said jacket; o. a chimney in communication with the interior of said furnace only to receive said gaseous products of combustion and discharge the same to the ambient atmosphere after said gaseous products of combustion have heated said heat exchanger; and p. fourth means for controlling the temperature of said heat exchanger to one at which said fluid is heated to the extent that said kiln is maintained at said first temperature at which substantially hydrogen chloride only is obtained from the partial decomposition of said plastic in said kiln.
Claim 3
Dependent Claim
109 words
An incinerator device as defined in claim 1 in which said first means comprises: q. a storage pit structure in which said scrap plastic is deposited; r. a power driven vibrating feeder; s. power means for moving said scrap plastic from said storage pit onto said vibrating feeder; t. a power driven crusher that receives said scrap plastic from said vibrating feeder and reduces said scrap in size; u. a bunker that receives said scrap plastic that has been reduced in size; and v. a power driven conveyor that moves said scrap plastic that has been reduced in size from said bunker to said first end of said kiln.
Claim 4
Dependent Claim
43 words
An incinerator device as defined in claim 1 which in addition includes: q. dust collecting means interposed between said furnace and chimney for removing particles of solids from said gaseous products of combustion prior to the latter being discharged to the ambient atmosphere.