33results about "Rotary retorts" patented technology

A system for processing solid waste including a segmented gasifier having a first segment detachably connected to a second segment, and a burner positioned downstream of the segmented gasifier and coupled to the segmented gasifier. A process for treating solid waste including introducing the solid waste into a first end of a segmented gasifier having a first segment detachably connected to a second segment. Gasifying the solid waste as it traverses from the first end of the gasifier to a second end of the segmented gasifier, and producing a gaseous output and a solid output at the second end of the segmented gasifier. Separating the gaseous output and the solid output, and introducing a portion of the gaseous output to a burner and recycling a portion of the gaseous output to the segmented gasifier as an energy source.

The invention discloses an internal structure of a straw shallow carbonization furnace, and relates to the field of carbonization furnaces, the internal structure comprises a carbonization assembly, one side of the carbonization assembly is provided with a transportation assembly, the upper end of the transportation assembly is provided with a pretreatment assembly, and the pretreatment assembly, the transportation assembly and the carbonization assembly are communicated with one another; the pretreatment assembly is fixedly connected to the upper portion of the conveying assembly, a through opening is formed in the top of the pretreatment assembly, a discharging hopper is arranged at the bottom of the pretreatment assembly, a feeding hopper is arranged at the top of the conveying assembly and matched with the discharging hopper, a heat dissipation chamber is arranged on the outer side of the pretreatment assembly, and a third motor is fixedly connected to the interior of the heat dissipation chamber. The output end of the third motor is fixedly connected with two groups of first gears, so that the subsequent carbonization reaction of the straws is more uniform; the size of straw is reduced, and the space utilization rate of transportation and storage is increased; the double-roller type crushing rollers meet the requirement of pretreatment granularity before straw shallow carbonization in a double-roller extruding and shearing mode.

The present disclosure provides systems and methods for efficiently converting whole tires into various commodity products, such as crude oil (e.g., West Texas Intermediate crude oil) and carbon that can be used in industrial processes such as steel manufacturing or further processed (e.g., activated) to form activated carbon.

The invention provides an agricultural modular container type organic solid waste carbonization system which comprises a container and an electromagnetic heating rotary carbonization furnace, and the electromagnetic heating rotary carbonization furnace is obliquely mounted in the container; the first annular heat preservation cover and the second annular heat preservation cover are arranged on the peripheries of the low-temperature section and the high-temperature section in a sleeving mode correspondingly; the first annular pretreatment box and the second annular pretreatment box are arranged in the first annular heat preservation cover and the second annular heat preservation cover respectively; and the rotary screening mechanism is used for synchronously driving the first annular pretreatment box and the second annular pretreatment box to rotate and swing front and back, and a tail gas treatment module and a remote controller are further integrally installed in the container. The system adopts a container type integration form, is short in construction period, low in cost, suitable for solid waste treatment scenes such as rural islands and the like, capable of combining drying, crushing and screening processes with a carbonization process, high in integration degree and capable of supporting remote parameter regulation and control of the Internet of Things.

A system is provided that enables a continuous process that involves the introduction of particles into a reactor drum having a low oxygen environment. Heavy hydrocarbons are boiled off of the particles during the heating of the particles. The boiled off heavy hydrocarbons mix with a heated gas stream that heats the particles within the reactor drum. The heated gas stream (with the boiled off heavy hydrocarbons) exit the drum and are recirculated back to a heat source for reheating the gas stream prior to reentering the reactor drum. Repeated exposure to the elevated temperatures within the reactor drum cracks the heavy hydrocarbons into lighter hydrocarbons. The lighter hydrocarbons may then be separated out of the heated gas stream and collected for sale or use.

A method of processing biomass is disclosed. The method includes providing biomass to a pyrolysis kiln, where the biomass has a moisture content of less than 40% and an ash content of less than 50%, and where the biomass has a biomass input temperature of less than 125°C. The method continues with heating at least an upstream portion of the pyrolysis kiln to maintain an upstream kiln temperature of between 800°C and 1250°C, and feeding the biomass through the pyrolysis kiln for a pyrolysis duration of 5 to 60 minutes to produce a kiln output that includes biocarbon and syngas. The biomass increases from the biomass input temperature to a biomass reaction temperature of at least 800°C in less than 25% of the pyrolysis duration. The method continues with discharging at least the biocarbon and the syngas from the pyrolysis kiln. Other methods and pyrolysis kilns are also disclosed.

The application provides an agricultural modular container type organic solid waste carbonization system, which comprises a container, an electromagnetic heating rotary carbonization furnace, a first annular pre-treatment box, a second annular pre-treatment box, a rotating screening mechanism, a tail gas treatment module and a remote controller.

The utility model relates to the technical field of pyrolysis carbonization's rotary furnace tube, disclose a kind of pyrolysis carbonization's rotary furnace tube of high efficiency, including rotary furnace tube, both ends in the rotary furnace tube are provided with three spiral structure, heat conduction groove is provided in the rotary furnace tube, one end of the rotary furnace tube is provided with spiral guide plate, the one end of spiral guide plate away from rotary furnace tube is connected with barrel three, the utility model reduces internal temperature difference, can effectively increase internal pyrolysis temperature, the arc design of heat conduction groove, can effectively replace material lifting plate, and reduce the raising of dust, the design of multiple heat conduction grooves, can effectively increase the strength of rotary furnace tube, prolong service life, avoid material return to smoke collection cover simultaneously.

The invention belongs to the technical field of agricultural and forestry waste recycling, and particularly relates to an agricultural and forestry organic waste incineration and carbonization integrated device which comprises a moving seat, a carbonization furnace is arranged at the top end of the moving seat, a carbonization pipe is rotationally connected into the carbonization furnace, a feeding pipe is fixed to the end, close to a picking machine, of the carbonization furnace, and a material distribution plate is arranged in the feeding pipe. A material distributing pipe is fixed to one side of the material distributing plate, a first screw rod is rotatably connected to the interior of the feeding pipe, the other end of the first screw rod is inserted into the carbonization pipe, and a second screw rod is rotatably connected to the interior of the material distributing pipe; a groove body is formed in the bottom end in the carbonization furnace, a pair of combustion plates are arranged in the groove body, and vent holes are formed in the top ends of the combustion plates; the picking machine is directly communicated with the carbonization furnace, so that the carbonization furnace can directly perform carbonization operation in a farmland, the carbonized raw materials are directly discharged to the farmland, an intermediate feeding link is not needed, and 20% of the raw materials can be used as fuel through material distribution of the material distribution plate, so that the fuel is saved.

The invention relates to providing a pyrolysis process for producing pyrolysis coke from organic material, which process functions continuously and is scalable. The pyrolysis takes place in a rotary kiln (2) by direct contact with a hot gas as the thermal transfer medium without the addition of an agent for partial oxidation, wherein the hot gas is generated in a combustion chamber (6) by combusting pyrolysis gas, wherein the combustion air is preheated in an air preheater (10) in order to ensure ignition. In the process, the hot gas is generated as a thermal transfer medium in a combustion chamber (6) by partially combusting a partial amount of the pyrolysis gas with a controllable amount of preheated air; is added to the rotary kiln at the coke discharge; and is conveyed through the rotary kiln counter to the flow of the material to be pyrolysed, the feedstock (1). The partial flow of pyrolysis gas to be partially combusted is removed from the overall flow immediately after the pyrolysis, that is to say after charging (3) the feedstock, and is conveyed by means of a conveyor element (5), steam ejector or mechanical fan to the combustion chamber (6). The air is pre-heated advantageously by the exhaust gas of the remainder of the pyrolysis gas to be combusted in the combustion chamber (7) in the flue-gas air pre-heater (10). The feedstock to be pyrolysed can be, but does not have to be, pre-dried.

The invention discloses a conveying device with an intelligent cooling function, and relates to the technical field of conveying devices. Comprising a control box, a first conveying cylinder, a second conveying cylinder, a driving assembly and a temperature control assembly, the control box is electrically connected with the driving assembly, and the first conveying cylinder and the second conveying cylinder are sleeved with each other and installed on the driving assembly; the discharging end of the first conveying cylinder is located in the second conveying cylinder, and the feeding end of the first conveying cylinder and the discharging end of the second conveying cylinder are located on the same side. The temperature control assembly comprises a temperature control cylinder and a heating part, the heating part is installed on the temperature control cylinder, the temperature control cylinder is inserted in the first conveying cylinder and the second conveying cylinder in a penetrating mode, the first conveying cylinder and the second conveying cylinder are driven to rotate through cooperation of the driving assembly, materials are conveyed in a U-shaped track, the required conveying length of the carbonization furnace is reduced, and the carbonization efficiency is improved. Heat loss is reduced, and heat utilization rate is improved.

This invention discloses a biomass pyrolysis reactor, comprising a feeding pipe, an inner reactor, and an outer reactor. The feeding pipe has a feed funnel at its front end. The feeding pipe, inner reactor, and outer reactor are mounted on the same mounting plate, with the rear end of the feeding pipe attached to the front end of the inner reactor. The rear half of the inner reactor is located inside the outer reactor. This design utilizes a first and second magnetic block to drive the outer and inner rings to rotate simultaneously during the rotation of the spiral conveyor blades. Simultaneously, a moving block repeatedly moves back and forth. Under the transmission of the first and second gears, the inner reactor can rotate repeatedly in both directions, thereby changing the direction of the centrifugal force on the hard, blocky biomass. This prevents the hard, blocky biomass from clogging the discharge port, improving the pyrolysis efficiency of the biomass.

This utility model discloses a vehicle-mounted carbonization device for processing biomass waste. The vehicle-mounted carbonization device includes a vehicle-mounted bracket, a carbonization unit, and a recovery unit. In the carbonization unit, the carbonization chamber is located inside a heat-conducting shell, which is installed inside an insulated box. The top surface of the carbonization chamber is open, and the rear is a door; at least half of the chamber can be removed from the rear side from the heat-conducting shell and the insulated box. The gap between the heat-conducting shell and the inner wall of the bottom of the insulated box serves as a combustion chamber, and the gap between the heat-conducting shell and other sides of the insulated box serves as a flue gas passage. The recovery unit is used to separate the effluent from the carbonization chamber, collect the produced liquid components, and send the produced fuel gas into the combustion chamber. The above-mentioned vehicle-mounted carbonization device can perform intermittent carbonization of various types of biomass waste and is easy to operate.

The utility model belongs to the field of carbonization equipment, and discloses a pyrolysis converter and a material taking device for the pyrolysis converter. The pyrolysis converter comprises a converter body, the converter body is in a transverse cylinder shape, a feeding port and a discharging port are formed in the two end faces of the converter body respectively, and the size of the feeding port is larger than the packaging size of materials used for being put into the pyrolysis converter; the material taking device for the pyrolysis converter is used for packaging and taking out reacted materials in the pyrolysis converter and comprises a material taking rod, the lower end of the material taking rod is fixedly connected with a bearing frame, the bottom of the bearing frame is provided with a rotating wheel used for enabling the material taking rod to move in the length direction of the bearing frame, and one end of the material taking rod is fixedly provided with a material taking rake in the height direction. According to the pyrolysis converter disclosed by the utility model, a material dismounting step and a special feeding device are omitted, the production steps are simplified, the production cost is reduced, and the material taking device disclosed by the utility model can be used for easily taking out the empty oil drum from the pyrolysis converter without manually taking out the empty oil drum from the pyrolysis converter, so that the pyrolysis converter is suitable for pyrolysis of materials.

The utility model relates to the technical field of sludge carbonization, in particular to a sludge carbonization device with a smoke recycling structure, which comprises a mounting base, a rotating shell is fixedly mounted on the outer surface of the mounting base, and a driving motor is fixedly mounted at one end, close to an electric push rod, of the rotating shell. And a rotating cylinder is rotationally mounted in the rotating shell. According to the sludge carbonization device with the flue gas recycling structure, after the combustion flame nozzle is started, sludge particles in the rotating cylinder are heated, the sludge particles are carbonized through heating, and at the moment, the sludge particles can generate a large amount of pyrolysis flue gas; pyrolysis flue gas is fed into the combustion flame nozzle to be combusted and used through starting of the gas suction pump, meanwhile, gas in a pipeline cannot flow back through the one-way valve, the pyrolysis flue gas generated when sludge particles are carbonized can be recycled, energy consumed when the sludge particles are carbonized is reduced, and the production cost is reduced.

The utility model discloses convection type rotary carbonization equipment which comprises a rotary furnace, when the rotary furnace rotates, a gear I on the surface of the rotary furnace rotates, a gear II meshed with the gear I drives a spiral conveying rod to rotate, and the spiral conveying rod rotates, so that materials in a shell move towards one side until the materials enter the rotary furnace through a material conveying pipe; an additional driving device is not used for rotation of the spiral conveying rod, so that the manufacturing cost is saved; when the rotary furnace exhausts high-temperature tail gas through the tail gas exhaust port, the tail gas enters the tail gas pretreatment box through the tail gas conveying pipe, then enters the main gas conveying pipeline from the tail gas pretreatment box and then reaches the ventilation port of the spiral conveying rod from the main gas conveying pipeline to heat the spiral conveying rod, and meanwhile, the tail gas enters the auxiliary gas conveying pipeline through the main gas conveying pipeline; tail gas heats the shell from the auxiliary gas conveying pipeline, materials are preheated through the temperature of the shell and the temperature of the spiral conveying rod, the production period is shortened, and the production efficiency is improved.

A bidirectional flow heating internal heating rotary carbonization furnace and its process control method are disclosed, relating to a carbonization apparatus. It includes a feeder, a bidirectional flow rotary kiln, a high-temperature gas duct, a discharge cabinet, a cooling carbon collector, a low-temperature gas duct, a medium-temperature gas duct, a two-stage combustion furnace, a high-temperature flue, and a circulating control piping system. Raw material carbonization undergoes two stages: a counter-current carbonization stage, mainly completed in the counter-current carbonization furnace section, where the raw material flows downwards and the flue gas flows upwards, and most of the moisture in the raw material is gasified in this stage; and a co-current carbonization stage, mainly completed in the co-current carbonization furnace section, where both the raw material and flue gas move downwards, and most of the organic matter in the raw material is decomposed in this stage. A process control method is provided, including ignition, heating, feeding carbonization, gas ring formation, two-stage combustion, energy self-supply, control of carbonization temperature, and control of gas flow rate. Compared with previous carbonization systems, this method omits the additional drying step, simplifies equipment, and ensures the stability of the carbonization effect.

The utility model discloses a mobile carbonization equipment for processing biomass waste. The mobile carbonization equipment comprises a trailer, a vehicle-mounted bracket, a carbonization unit, a recovery unit and a purification unit. In the carbonization unit, a carbonization bin is located in a heat-conducting shell, and the heat-conducting shell is installed in a heat preservation box. The top surface of the carbonization bin is open, and the back surface is a bin door. At least one half of the carbonization bin can be removed from the back side of the heat-conducting shell and the heat preservation box. The space between the heat-conducting shell and the inner wall of the bottom surface of the heat preservation box serves as a combustion chamber, and the space between the heat-conducting shell and the other side surfaces of the heat preservation box serves as a flue gas passage. The recovery unit is used for separating the escaping substances of the carbonization bin, collecting the prepared liquid components, and sending the prepared fuel gas into the combustion chamber. The purification unit is used for treating flue gas. The above-mentioned mobile carbonization equipment can intermittently carbonize various types of biomass waste, and is convenient to operate.

The invention relates to the technical field of activated carbon preparation, and provides a carbonization furnace for activated carbon production, which comprises a carbonization furnace main body rotationally arranged in a combustion chamber, and a plurality of partition plates arranged in the carbonization furnace main body along the radial direction of the carbonization furnace main body, a material passing interval through which materials can pass is formed between one end, far away from the axis of the carbonization furnace main body, of each partition plate and the inner wall of the carbonization furnace main body, the multiple partition plates are distributed at intervals in the circumferential direction, a material storage space is formed between every two adjacent partition plates, and the multiple material storage spaces are communicated through the material passing intervals; and the flexible part is annular and is arranged on the peripheries of the partition plates in a sleeving mode, and the materials press part of the flexible part into the material storage space. By means of the technical scheme, the problems that in the prior art, materials are prone to being damaged in the rotation process, material overturning and flowing are weakened, and overall consistency of the materials is not facilitated are solved.

The present application relates to biomass carbonization equipment technical field, specifically to a kind of biomass carbonization reaction device and method, including heat conduction ventilation structure and carbonization reaction structure, and the heat conduction ventilation structure is connected with carbonization reaction structure.The structure of carbonization reaction structure is set, the purpose of carbonization processing is realized, gas is introduced into heat insulation sleeve through docking vent, guiding shunt pipe, communication branch pipe, and speed reducer is rotated by second matching gear disc to drive first matching gear disc, so that drive transmission rod is rotated by telescopic connecting rod to drive storage seat, mixed rotation purpose is realized, continuous carbonization production work is realized, and heating resistance is heated by electrification, the heating carbonization treatment work of biomass raw material in storage seat is realized, and the purpose of automatic processing production is facilitated.

Disclosed herein are systems for pyrolysis of plastic feedstock comprising post-consumer and / or post-industrial plastics and method of using the same. In various implementations, the systems include a reactor having a reactor vessel for receiving and pyrolyzing the plastic feedstock, and a solids separation system configured for separating at least a portion of the solids present in the reactor bath from the reactor bath.

A method of processing biomass is disclosed. The method includes providing biomass to a pyrolysis kiln, where the biomass has a moisture content of less than 40% and an ash content of less than 50%, and where the biomass has a biomass input temperature of less than 125° C. The method continues with heating at least an upstream portion of the pyrolysis kiln to maintain an upstream kiln temperature of between 800° C. and 1250° C., and feeding the biomass through the pyrolysis kiln for a pyrolysis duration of 5 to 60 minutes to produce a kiln output that includes biocarbon and syngas. The biomass increases from the biomass input temperature to a biomass reaction temperature of at least 800° C. in less than 25% of the pyrolysis duration. The method continues with discharging at least the biocarbon and the syngas from the pyrolysis kiln. Other methods and pyrolysis kilns are also disclosed.

The invention relates to the technical field of biomass energy conversion, in particular to an environment-friendly machine-made charcoal carbonization system which comprises a shell, a feeding port is formed in the outer wall of the upper end of the shell, a motor is fixedly connected to the periphery of the top of the shell, and a heat removal pipeline is communicated with the center of the top of the shell. The bottom of the shell is fixedly connected with a carbonization chamber, the inner wall of the shell is fixedly connected with a heat insulation cover, and the inner side of the shell is provided with a flue; a first gear is driven by a motor to rotate, and the effect that the first gear drives a rotating part and a carbonization pipe to rotate and revolve is utilized, so that it is guaranteed that heat is evenly received in the carbonization device, and carbonization completeness and thoroughness can be achieved; a fourth gear and a reciprocating threaded rod are driven through a rotary disc and a rack, so that an upper sliding block moves downwards to be matched with a lower sliding block for shaping, and shaping of machine-made charcoal is completed along with carbonization of materials.

The invention discloses a sludge drying and carbonizing integrated furnace and a sludge treatment method, and relates to the technical field of sludge treatment.The sludge drying and carbonizing integrated furnace comprises a furnace body, and a combustion space and a sludge treatment space are defined in the furnace body; and the discharging switching device is configured to send the sludge into the combustion space or send the sludge out of the furnace body. The combustion space and the sludge treatment space are arranged in the furnace body, sludge can be quickly dried and carbonized, and the carbonized sludge is fed into the combustion space for combustion by utilizing the discharging switching device, so that pyrolysis oil gas generated in the drying and carbonization process is solved; and the carbon residues formed after sludge drying and carbonization are fed into combustion, so that the energy consumption can be reduced, the sludge discharge amount can be reduced, the dried and carbonized carbon residues can be discharged as required, and the application mode is flexible.

To provide a carbonization apparatus that enables efficient and stable carbonization while also being environmentally friendly. [Solution] The carbonization apparatus 1 comprises a kiln 10 having a hexagonal cylindrical kiln shell 11, a carbon heater 30 disposed inside the kiln shell 11, and a drive unit 20 that rotates the kiln shell 11; an input unit 50 disposed at one end of the kiln shell 11 for introducing food residue into the kiln shell 11; and an output unit 51 disposed at the other end of the kiln shell 11 for discharging food residue that has passed through the inside of the kiln shell 11. The kiln shell 11 has a cross-sectional shape of a regular hexagon, and the drive unit 20 rotates the kiln shell 11 at a speed that causes the food residue to slide down along the inner wall of the kiln shell 11 in the opposite direction to the rotation direction of the kiln shell 11 before it reaches the top inside the kiln shell 11.

The process and the equipment that continuously integrates the pyrolysis processes in a Rotary kiln at average temperatures of 300 to 500°C with a gasifier on moving grates in average temperatures of 500 to 800°C, whose purpose is to produce a mixture of gases originating from the pyrolysis and gasification processes of waste and their derivatives. In this process, the gas mixture known as "Waste-Derived Combustible Gases (WDCG) is continuously drawn through a Venturi system or an exhaust system, and can be directed to a combustion system or treatment and separation of combustible fractions for subsequent energy recovery. From this process and its unprecedented processing characteristics, powdered, fine, sludge, pasty or liquid waste can be thermally treated individually or in blends with other waste such as urban, commercial or industrial solid waste, with additional energy recovery.

The invention discloses a multi-layer staggered composite biomass rotary carbonization device which comprises a multi-layer composite rotary kiln, a feeding mechanism, a carbon discharging mechanism, a heating gas path, a gas combustion furnace, a cracking gas path and waste heat utilization equipment, the multi-layer composite rotary kiln at least comprises ten layers from outside to inside, namely a protective layer, a heat preservation layer, a shell outer layer, a shell layer, a shell inner layer, a material layer, a pipe outer layer, a pipe layer, a pipe inner layer and a material core layer. Wherein the shell layer and the pipe layer are heating layers, and heating gas is introduced into the heating layers; the material layer and the material core layer are raw material layers and contain raw materials, carbonized materials and pyrolysis gas; and the shell layer, the material layer, the pipe layer and the material core layer form four-layer staggered composite distribution of heating, raw material heating and raw material heating. The heat exchange area of the carbonization device is effectively increased, the heating efficiency and the productivity are improved, and a technical guarantee is provided for large-scale preparation of carbonized materials.

The application discloses a segmented biomass continuous drying pyrolysis carbonization equipment and relates to the field of carbonization furnaces.The equipment comprises a supporting unit, the supporting unit comprises a supporting frame horizontally laid on the ground, a heating box is fixedly installed on the top of the supporting frame, and the heating box is sleeved with the outside of a part of raw material carbonization units.The segmented biomass continuous drying pyrolysis carbonization equipment takes the supporting unit as the basis, the horizontally laid supporting frame bears the heating box and the raw material carbonization units, and the carbonization furnace is provided with stable rotating support through the mounting seat and the rollers, so that the stable operation of the equipment is ensured.The raw material carbonization unit is a core part, the carbonization furnace is segmented heated in the heating box, the temperature gradient of preheating, carbonization and cooling is formed, the spiral protrusions in the carbonization furnace push the biomass materials to move forward, uniform heating and sufficient stirring are simultaneously realized, and the pyrolysis reaction is promoted.

Methods and apparatus may permit the generation of consistent output synthesis gas from highly variable input feedstock solids carbonaceous materials. A stoichiometric objectivistic chemic environment may be established to stoichiometrically control carbon content in a solid carbonaceous materials gasifier system. Processing of carbonaceous materials may include dominative pyrolytic decomposition and multiple coil carbonaceous reformation. Dynamically adjustable process determinative parameters may be utilized to refine processing, including process utilization of negatively electrostatically enhanced water species, process utilization of flue gas, and adjustment of process flow rate characteristics. Recycling may be employed for internal reuse of process materials, including recycled negatively electrostatically enhanced water species, recycled flue gas, and recycled contaminants. Synthesis gas generation may involve predetermining a desired synthesis gas for output and creating high yields of such a predetermined desired synthesis gas.

To provide pyrolysis, roasting, and / or gasification systems and methods. [Solution] A system is provided that enables a continuous process involving the introduction of particles into a reactor drum having a low-oxygen environment. Heavy hydrocarbons are boiled off from the particles during heating of the particles. The boiled-off heavy hydrocarbons are mixed with a heated gas stream that heats the particles in the reactor drum. The heated gas stream (with the boiled-off heavy hydrocarbons) is recirculated back to the heat source to reheat the gas stream before leaving the drum and re-entering the reactor drum. Repeated exposure to high temperatures in the reactor drum decomposes the heavy hydrocarbons into lighter hydrocarbons. The lighter hydrocarbons are then separated out of the heated gas stream and can be collected for sale or use.