CN104449791A - Peristaltic solid-phase reactor and combined module - Google Patents

Peristaltic solid-phase reactor and combined module Download PDF

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Publication number
CN104449791A
CN104449791A CN201410640516.2A CN201410640516A CN104449791A CN 104449791 A CN104449791 A CN 104449791A CN 201410640516 A CN201410640516 A CN 201410640516A CN 104449791 A CN104449791 A CN 104449791A
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CN
China
Prior art keywords
phase reactor
solid phase
furnace body
type solid
feed
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CN201410640516.2A
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Chinese (zh)
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CN104449791B (en
Inventor
时俊
陈鸽飞
陆维
陶明华
朱宏明
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Changshu Mocheng Development And Construction Co ltd
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CHANGSHU HIGH PRESSURE VESSEL MANUFACTURING Co Ltd
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Classifications

    • CCHEMISTRY; METALLURGY
    • C10PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10GCRACKING HYDROCARBON OILS; PRODUCTION OF LIQUID HYDROCARBON MIXTURES, e.g. BY DESTRUCTIVE HYDROGENATION, OLIGOMERISATION, POLYMERISATION; RECOVERY OF HYDROCARBON OILS FROM OIL-SHALE, OIL-SAND, OR GASES; REFINING MIXTURES MAINLY CONSISTING OF HYDROCARBONS; REFORMING OF NAPHTHA; MINERAL WAXES
    • C10G1/00Production of liquid hydrocarbon mixtures from oil-shale, oil-sand, or non-melting solid carbonaceous or similar materials, e.g. wood, coal
    • CCHEMISTRY; METALLURGY
    • C10PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10BDESTRUCTIVE DISTILLATION OF CARBONACEOUS MATERIALS FOR PRODUCTION OF GAS, COKE, TAR, OR SIMILAR MATERIALS
    • C10B47/00Destructive distillation of solid carbonaceous materials with indirect heating, e.g. by external combustion
    • C10B47/28Other processes
    • C10B47/30Other processes in rotary ovens or retorts
    • CCHEMISTRY; METALLURGY
    • C10PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10BDESTRUCTIVE DISTILLATION OF CARBONACEOUS MATERIALS FOR PRODUCTION OF GAS, COKE, TAR, OR SIMILAR MATERIALS
    • C10B47/00Destructive distillation of solid carbonaceous materials with indirect heating, e.g. by external combustion
    • C10B47/28Other processes
    • C10B47/32Other processes in ovens with mechanical conveying means
    • C10B47/34Other processes in ovens with mechanical conveying means with rotary scraping devices
    • CCHEMISTRY; METALLURGY
    • C10PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10BDESTRUCTIVE DISTILLATION OF CARBONACEOUS MATERIALS FOR PRODUCTION OF GAS, COKE, TAR, OR SIMILAR MATERIALS
    • C10B53/00Destructive distillation, specially adapted for particular solid raw materials or solid raw materials in special form

Abstract

The invention discloses a peristaltic solid-phase reactor comprising a furnace body, wherein the furnace body comprises a central tube and an outer cover body capable of rotationally sleeving the outer part of the central tube; an annular cavity capable of storing garbage is formed between the inner wall of the outer cover body and the outer wall of the central tube; one end of the furnace body is provided with a feeding unit, and the other end of the furnace body is provided with a discharging unit; a supporting unit is arranged below the furnace body; the furnace body is obliquely arranged, and the end, which is provided with the feeding unit, of the furnace body, is higher than the end provided with the discharging unit; the inner wall of the outer cover body is provided with a plurality of blades capable of conveying garbage; and an intermittent spiral line is formed at the circumferential inner ends of the blades. Due to the adoption of a cracking furnace designed by the invention, the aim of preliminarily decomposing the garbage is achieved; the peristaltic solid-phase reactor is reasonable in structure and convenient to overhaul; the furnace body is obliquely arranged, so that the garbage can be smoothly and completely discharged, and the efficiency is increased while the quality is ensured; and a module with the reactor can be used for cracking the garbage into gas, oil and charcoal and realizing the processes of changing waste materials into things of value and regenerating energy sources so as to be suitable for popularization and application.

Description

A kind of creeping motion type solid phase reactor and combined type module
Technical field
The present invention relates to a kind of creeping motion type solid phase reactor and combined type module.
Background technology
Current is burn and landfill to the main processing ways of domestic waste.Burn and belong to crushing processing mode, by burning, rubbish is become flue gas and discharge, residue is undertaken buried by the solid standard of danger after collecting, and the heat that burning produces is by steam conversion power generation, but this mode processing cost is expensive, and smoke gas treatment requires high; Landfill belongs to hidden type processing mode, realizes the disappearance of rubbish by rotting for a long time, but can produce a large amount of harmful sewage due to rotten organism and take a large amount of soils, is also difficult at present continue to carry out on a large scale in application.Therefore, find new refuse treatment scheme, the harmless treatment realizing domestic refuse has been current city development and management " just needing ".
Summary of the invention
The object of this invention is to provide a kind of creeping motion type solid phase reactor and combined type module, a kind of novel refuse treatment plant, by these creeping motion type solid phase reactors, cracking is layer by layer carried out to rubbish, generate gas, oil, charcoal, be one turn waste into wealth, the process of energy regeneration, device structure is reliable, and efficiency is high, and be convenient to safeguard and maintenance, be suitable for applying in field of garbage disposal.
For solving the problems of the technologies described above, the present invention adopts following technical scheme:
A kind of creeping motion type solid phase reactor, comprise furnace body, described furnace body comprises pipe core, the outer outlet body of described pipe core outside can be set in rotationally, the annular chamber can receiving rubbish is formed between the inwall of described outer outlet body and the outer wall of described pipe core, one end of described furnace body is provided with feed unit, the other end is provided with discharging unit, the below of described furnace body is provided with support unit, described furnace body is obliquely installed, and the one end being provided with described feed unit is higher than the one end being provided with described discharging unit, the inwall of described outer outlet body is provided with multi-disc can the blade of conveying garbage, circumference the inner of blade described in these forms interrupted spiral-line.
Preferably, described feed unit comprises the material feeding box with opening for feed, and the inside of described material feeding box forms feed cavity, and described feed cavity and described annular chamber connect.
Preferably, the charging scraper plate that the rubbish be attached on the inwall of described material feeding box can be scraped off is provided with in described feed cavity.
Preferably, described discharging unit comprises the feed box with discharge port, and the inside of described feed box forms discharging chamber, and described discharging chamber and described annular chamber connect.
Preferably, the discharging scraper plate that the rubbish be attached on the inwall of described feed box can be scraped off is provided with in described discharging chamber.
Preferably, described support unit comprises the second support portion near the first support portion of described feed unit, near described discharging unit.
Preferably, this creeping motion type solid phase reactor also comprises the driver element that described outer outlet body can be driven to rotate, described driver element comprises follower gear on the outer wall being circumferentially arranged on described outer outlet body, the driving toothed gear that arranges with described follower gear phase external toothing, drive described in the motor component that rotates of driving toothed gear.
Preferably, described outer outlet body offers inspection port, and the position of described inspection port is provided with the inspection door that can open or close.
A kind of combined type module, comprise the pretreatment unit that rubbish is carried out preliminary examination and put in storage, rubbish is carried out to the resolving cell of disaggregating treatment, the post-processing unit that the product obtained described resolving cell is separated and collects, described resolving cell comprises the preorder reactor and multiple subsequent reactor of connecting successively, described preorder reactor is the above-mentioned creeping motion type solid phase reactor of any one, the rubbish that described pretreatment unit is sent enters described resolving cell from the opening for feed of described preorder reactor, the mixture that the discharge port of the subsequent reactor in described resolving cell described in last is sent enters in described post-processing unit.
Preferably, described resolving cell comprises the subsequent reactor described in three.
Beneficial effect of the present invention is: realized the object of tentatively decomposing rubbish by the creeping motion type solid phase reactor of the design, rational in infrastructure, maintenance is convenient, and furnace body is obliquely installed, ensure rubbish smoothly, fully discharging, raise the efficiency while ensuring the quality of products, adopt the combined type module of this reactor can be gas, oil, charcoal by garbage cracking, be one turn waste into wealth, the process of energy regeneration, be suitable for applying.
Accompanying drawing explanation
the structural representation of four creeping motion type solid phase reactors that the resolving cell that accompanying drawing 1 to accompanying drawing 4 is respectively the present embodiment comprises, each accompanying drawing is skeleton view;
accompanying drawing 5 is the process flow diagram of the combined type module of the present embodiment.
in accompanying drawing: 101, pipe core; 102, outer outlet body; 103, feed unit; 104, discharging unit; 105, material feeding box; 106, charging scraper plate; 107, feed box; 108, discharging scraper plate; 109, the first support portion; 110, the second support portion; 111, follower gear; 112, driving toothed gear; 113, motor component; 114, inspection door; 201, outer cylinder body; 202, stir shaft; 203, opening for feed; 204, discharging bin; 205, shuttle element; 206, axis body; 210, front end-plate; 211, back head; 212, first goes out material for making clothes storehouse; 213, second goes out material for making clothes storehouse; 301, blade.
Embodiment
Below in conjunction with the drawings and specific embodiments, illustrate the present invention further, these embodiments should be understood only be not used in for illustration of the present invention and limit the scope of the invention, after having read the present invention, the amendment of those skilled in the art to the various equivalent form of value of the present invention has all fallen within the application's claims limited range.
As shown in Figure 1, a kind of creeping motion type solid phase reactor, comprise furnace body, furnace body comprises pipe core 101, the outer outlet body 102 of pipe core 101 outside can be set in rotationally, the annular chamber can receiving rubbish is formed between the inwall of outer outlet body 102 and the outer wall of pipe core 101, one end of furnace body is provided with feed unit 103, the other end is provided with discharging unit 104, the below of furnace body is provided with support unit, furnace body is obliquely installed, and the one end being provided with feed unit 103 is higher than the one end being provided with discharging unit 104, the inwall of outer outlet body 102 is provided with multi-disc can the blade 301 of conveying garbage, circumference the inner of these blades 301 forms interrupted spiral-line, more specifically, feed unit 103 comprises the material feeding box 105 with opening for feed 203, the inside of material feeding box 105 forms feed cavity, feed cavity and annular chamber connect, the charging scraper plate 106 that the rubbish be attached on the inwall of material feeding box 105 can be scraped off is provided with in feed cavity, discharging unit 104 comprises the feed box 107 with discharge port, the inside of feed box 107 forms discharging chamber, discharging chamber and annular chamber connect, the discharging scraper plate 108 that the rubbish be attached on the inwall of feed box 107 can be scraped off is provided with in discharging chamber, support unit comprises the first support portion 109 near feed unit 103, near the second support portion 110 of discharging unit 104, this creeping motion type solid phase reactor also comprises the driver element that outer outlet body 102 can be driven to rotate, driver element comprises the follower gear 111 on the outer wall being circumferentially arranged on outer outlet body 102, the driving toothed gear 112 arranged with the external toothing of follower gear 111 phase, drive the motor component 113 that driving toothed gear 112 rotates, outer outlet body 102 offers inspection port, and the position of inspection port is provided with the inspection door 114(and manhole that can open or close), the service temperature of this creeping motion type solid phase reactor is no more than 150 degree, atmospheric operation, general carbon steel is selected to make, its material feeding box 105, feed box 107 and furnace body disconnect completely, and the gap keeping certain seals, rubbish, under the drive of gear, with extremely low rotational speed, is pushed by the blade 301 of inwall, carries out preliminary Reaction Separation by furnace body inchmeal.
Creeping motion type solid phase reactor as shown in Figure 2, comprise furnace body, furnace body comprises outer cylinder body 201, coaxially be arranged on the stir shaft 202 in outer cylinder body 201, drive the driver element that stir shaft 202 rotates, formed between the inwall of outer cylinder body 201 and stir shaft 202 and move for material the reaction chamber passed through, one end of outer cylinder body 201 is provided with opening for feed 203, the other end is provided with discharging bin 204, discharging bin 204 comprises the feed box 107 with discharge port, discharging chamber is formed in feed box 107, discharging chamber and reaction chamber connect, more specifically, the axis body 206 that stir shaft 202 comprises center and the blade 301 be arranged on the outer wall of axis body 206, these blades 301 of corresponding opening for feed 203 part are obliquely installed and axially incline angle is 20 °, all the other blades 301 are also obliquely installed and axially incline angle is 10 °, the discharging scraper plate 108 that the material scraper be attached on the inwall of feed box 107 can be got off is provided with in discharging chamber, the axially incline angle of discharging scraper plate 108 is 0 °, the end part seal away from discharging bin 204 of outer cylinder body 201 is provided with front end-plate 210, the end away from outer cylinder body 201 of discharging bin 204 is provided with back head 211, part stir shaft 202 stretches out outside front end-plate 210, driver element comprises the follower gear 111 on the stir shaft 202 that is arranged on and stretches out outside front end-plate 210, with the driving toothed gear 112 of follower gear 111 engaged transmission, drive the motor component 113 that driving toothed gear 112 rotates.
Creeping motion type solid phase reactor as shown in Figure 3 with shown in accompanying drawing 2 the structure of creeping motion type solid phase reactor identical, but contrary shown in the placement direction of feed end and discharge end and accompanying drawing 2.
The operating pressure of accompanying drawing 2 and the creeping motion type solid phase reactor shown in accompanying drawing 3 is 0.05MPa, working temperature is 250 ~ 300 DEG C, employing low alloy steel makes, the rotating speed of stir shaft 202 is less than 2rpm, pushed by the 301 pairs of materials of the blade on stir shaft 202, the reaction times in stove can be controlled by the rotating speed adjusting stir shaft 202.
Creeping motion type solid phase reactor as shown in Figure 4, comprise furnace body, furnace body comprises outer cylinder body 201, coaxially be arranged on the stir shaft 202 in outer cylinder body 201, drive the driver element that stir shaft 202 rotates, formed between the inwall of outer cylinder body 201 and stir shaft 202 and move for material the reaction chamber passed through, one end of outer cylinder body 201 is provided with opening for feed 203, the other end is provided with discharging bin 204, discharging bin 204 comprises the feed box 107 with discharge port, discharging chamber is formed in feed box 107, the shuttle element 205 that can open or close is provided with between discharging chamber and reaction chamber, when shuttle element 205 is in open mode, reaction chamber and discharging chamber connect, when shuttle element 205 is in closing condition, reaction chamber cuts off mutually with discharging chamber, more specifically, the axis body 206 that stir shaft 202 comprises center and the blade 301 be arranged on the outer wall of axis body 206, these blades 301 of corresponding opening for feed 203 part are obliquely installed and axially incline angle is 15 °, all the other blades 301 are also obliquely installed and axially incline angle is 6 °, the discharging scraper plate 108 that the material scraper be attached on the inwall of feed box 107 can be got off is provided with in discharging chamber, the axially incline angle of discharging scraper plate 108 is 0 °, shuttle element 205 comprises upper plate, middle plate and lower plate, middle plate is fixedly installed between discharging chamber and reaction chamber, upper plate, lower plate can be arranged on to lifting moving the both sides of middle plate respectively, the end part seal away from discharging bin 204 of outer cylinder body 201 is provided with front end-plate 210, the end away from outer cylinder body 201 of discharging bin 204 is provided with back head 211, part stir shaft 202 stretches out outside front end-plate 210, driver element comprises the follower gear 111 on the stir shaft 202 that is arranged on and stretches out outside front end-plate 210, with the driving toothed gear 112 of follower gear 111 engaged transmission, drive the motor component 113 that driving toothed gear 112 rotates, discharging bin 204 comprises first of axial array and goes out material for making clothes storehouse 212 and second and go out material for making clothes storehouse 213, first goes out material for making clothes storehouse 212 to the second goes out material for making clothes storehouse 213 near reaction chamber, first goes out material for making clothes storehouse 212 and second goes out between material for making clothes storehouse 213 to be also provided with shuttle element 205, shuttle element 205 comprises upper plate, middle plate and lower plate, middle plate is fixedly installed between discharging chamber and reaction chamber, upper plate, lower plate can be arranged on to lifting moving the both sides of middle plate respectively, the rotating speed of the stir shaft 202 in this creeping motion type solid phase reactor is about 1rpm, rotating speed equally by adjusting stir shaft 202 controls the reaction times of material in stove, this in-furnace temperature height 600 DEG C, therefore the temperature distortion amount of middle outer cylinder body 201 of working is larger, adjust by following sliding pair, thus ensure the real-time support of support component.
The below of accompanying drawing 2, accompanying drawing 3 and the creeping motion type solid phase reactor shown in accompanying drawing 4 is provided with support component, to ensure that the axle center of creeping motion type solid phase reactor is in horizontality, and ensure the support of extending larger body of heater, and below support component, there is sliding pair, be convenient to move body of heater or stretch, and the outer cylinder body 201 of these three creeping motion type solid phase reactors is also provided with inspection door 114(and manhole).
A kind of resolving cell, comprise accompanying drawing 1, accompanying drawing 2, accompanying drawing 3 and the creeping motion type solid phase reactor of four shown in accompanying drawing 4, wherein, the discharge port of the creeping motion type solid phase reactor shown in accompanying drawing 1 is communicated to the opening for feed 203 of the creeping motion type solid phase reactor shown in accompanying drawing 2, the discharge port of the creeping motion type solid phase reactor shown in accompanying drawing 2 is communicated to the opening for feed 203 of the creeping motion type solid phase reactor shown in accompanying drawing 3, the discharge port of the creeping motion type solid phase reactor shown in accompanying drawing 3 is communicated to the opening for feed 203 of the creeping motion type solid phase reactor shown in accompanying drawing 4, rubbish enters this resolving cell through conveying belt from the opening for feed 203 of the creeping motion type solid phase reactor shown in accompanying drawing 1.
As shown in Figure 5, a kind of combined type module, comprise the post-processing unit that the product that carries out preliminary examination and the pretreatment unit put in storage to rubbish, rubbish carried out to the resolving cell of disaggregating treatment, obtain resolving cell is separated and collects, resolving cell is as above-mentioned, the rubbish that pretreatment unit is sent enters in resolving cell, and the mixture that in resolving cell, the discharge port of last creeping motion type solid phase reactor is sent enters in post-processing unit; The needs of certain degree of decomposition can increase and decrease the quantity of creeping motion type solid phase reactor in resolving cell; Rubbish is mainly placed in the position of formulation by above-mentioned pretreatment unit according to classification and demand, and is carried by rubbish by conveying; Under the cracking process effect of resolving cell, garbage decomposition is the mixture of gas, oil, charcoal, slag etc.; This mixture enters in post-processing unit and is respectively separated and collects, thus completes process.
These creeping motion type solid phase reactors, rational in infrastructure, maintenance convenience, raises the efficiency while ensuring the quality of products, adopts the module of this creeping motion type solid phase reactor can be gas, oil, charcoal by garbage cracking, be one turn waste into wealth, the process of energy regeneration, be suitable for applying.
The above is only the preferred embodiment of the present invention; it should be pointed out that for those skilled in the art, under the premise without departing from the principles of the invention; can also make some improvements and modifications, these improvements and modifications also should be considered as protection scope of the present invention.

Claims (10)

1. a creeping motion type solid phase reactor, it is characterized in that: comprise furnace body, described furnace body comprises pipe core, the outer outlet body of described pipe core outside can be set in rotationally, the annular chamber can receiving rubbish is formed between the inwall of described outer outlet body and the outer wall of described pipe core, one end of described furnace body is provided with feed unit, the other end is provided with discharging unit, the below of described furnace body is provided with support unit, described furnace body is obliquely installed, and the one end being provided with described feed unit is higher than the one end being provided with described discharging unit, the inwall of described outer outlet body is provided with multi-disc can the blade of conveying garbage, circumference the inner of blade described in these forms interrupted spiral-line.
2. creeping motion type solid phase reactor according to claim 1, is characterized in that: described feed unit comprises the material feeding box with opening for feed, and the inside of described material feeding box forms feed cavity, and described feed cavity and described annular chamber connect.
3. creeping motion type solid phase reactor according to claim 1, is characterized in that: be provided with the charging scraper plate that the rubbish be attached on the inwall of described material feeding box can be scraped off in described feed cavity.
4. creeping motion type solid phase reactor according to claim 1, is characterized in that: described discharging unit comprises the feed box with discharge port, and the inside of described feed box forms discharging chamber, and described discharging chamber and described annular chamber connect.
5. creeping motion type solid phase reactor according to claim 1, is characterized in that: be provided with the discharging scraper plate that the rubbish be attached on the inwall of described feed box can be scraped off in described discharging chamber.
6. creeping motion type solid phase reactor according to claim 1, is characterized in that: described support unit comprises the second support portion near the first support portion of described feed unit, near described discharging unit.
7. creeping motion type solid phase reactor according to claim 1, the driving toothed gear it is characterized in that: this creeping motion type solid phase reactor also comprises the driver element that described outer outlet body can be driven to rotate, described driver element comprises follower gear on the outer wall being circumferentially arranged on described outer outlet body, arranging with described follower gear phase external toothing, drive described in the motor component that rotates of driving toothed gear.
8. creeping motion type solid phase reactor according to claim 1, it is characterized in that: described outer outlet body offers inspection port, and the position of described inspection port is provided with the inspection door that can open or close.
9. a combined type module, it is characterized in that: comprise the pretreatment unit that rubbish is carried out preliminary examination and put in storage, rubbish is carried out to the resolving cell of disaggregating treatment, the post-processing unit that the product obtained described resolving cell is separated and collects, described resolving cell comprises the preorder reactor and multiple subsequent reactor of connecting successively, described preorder reactor is creeping motion type solid phase reactor as claimed in any of claims 1 to 8 in one of claims, the rubbish that described pretreatment unit is sent enters described resolving cell from the opening for feed of described preorder reactor, the mixture that the discharge port of the subsequent reactor in described resolving cell described in last is sent enters in described post-processing unit.
10. combined type module according to claim 9, is characterized in that: described resolving cell comprises the subsequent reactor described in three.
CN201410640516.2A 2014-11-13 2014-11-13 A kind of creeping motion type solid phase reactor and combined type module Active CN104449791B (en)

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Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN106147808A (en) * 2016-08-31 2016-11-23 苏州绿岛环保设备制造有限公司 The useless solid resource conversion technique of a kind of environmental protection
CN106675593A (en) * 2017-03-17 2017-05-17 上海亚泰仪表有限公司 Self-balanced non-quantification biomass treatment system and control method
CN106957665A (en) * 2017-04-11 2017-07-18 苏州绿岛环保设备制造有限公司 A kind of power transmission shaft for creeping motion type solid phase reactor

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CN101445737A (en) * 2008-12-31 2009-06-03 合肥工业大学 Internal combustion type heating rotating cone type biomass pyrolysis liquefaction device
US20110019981A1 (en) * 2009-07-21 2011-01-27 Ifp Rotary furnace for radiative heat treatment of solids
CN102212377A (en) * 2011-05-13 2011-10-12 安徽禾盛生物能源有限公司 Spiral biomass pyrolysis reactor with drying function
CN102703106A (en) * 2012-06-25 2012-10-03 徐效奇 Instant cracking reaction device adopting high-frequency heating and converting oil into membrane
CN203715567U (en) * 2014-01-16 2014-07-16 华北电力大学 Rolling type biomass pyrolysis poly-generation device

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Publication number Priority date Publication date Assignee Title
CN101134899A (en) * 2006-08-28 2008-03-05 李延韬 Biomass energy converter
CN101445737A (en) * 2008-12-31 2009-06-03 合肥工业大学 Internal combustion type heating rotating cone type biomass pyrolysis liquefaction device
US20110019981A1 (en) * 2009-07-21 2011-01-27 Ifp Rotary furnace for radiative heat treatment of solids
CN102212377A (en) * 2011-05-13 2011-10-12 安徽禾盛生物能源有限公司 Spiral biomass pyrolysis reactor with drying function
CN102703106A (en) * 2012-06-25 2012-10-03 徐效奇 Instant cracking reaction device adopting high-frequency heating and converting oil into membrane
CN203715567U (en) * 2014-01-16 2014-07-16 华北电力大学 Rolling type biomass pyrolysis poly-generation device

Cited By (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN106147808A (en) * 2016-08-31 2016-11-23 苏州绿岛环保设备制造有限公司 The useless solid resource conversion technique of a kind of environmental protection
CN106675593A (en) * 2017-03-17 2017-05-17 上海亚泰仪表有限公司 Self-balanced non-quantification biomass treatment system and control method
CN106675593B (en) * 2017-03-17 2020-07-03 上海亚泰仪表有限公司 Self-balancing non-quantitative biomass processing system and control method
CN106957665A (en) * 2017-04-11 2017-07-18 苏州绿岛环保设备制造有限公司 A kind of power transmission shaft for creeping motion type solid phase reactor
CN106957665B (en) * 2017-04-11 2018-04-17 苏州绿岛环保设备制造有限公司 A kind of transmission shaft for creeping motion type solid phase reactor

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