CN104941960A - Granular-substance cooling and cleaning fluidized bed - Google Patents

Granular-substance cooling and cleaning fluidized bed Download PDF

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Publication number
CN104941960A
CN104941960A CN201510302931.1A CN201510302931A CN104941960A CN 104941960 A CN104941960 A CN 104941960A CN 201510302931 A CN201510302931 A CN 201510302931A CN 104941960 A CN104941960 A CN 104941960A
Authority
CN
China
Prior art keywords
fluid bed
granular
air
bed surface
particulate material
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Pending
Application number
CN201510302931.1A
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Chinese (zh)
Inventor
不公告发明人
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Anhui Vast Foreign-Festival Energy Science And Technology Ltd
Original Assignee
Anhui Vast Foreign-Festival Energy Science And Technology Ltd
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by Anhui Vast Foreign-Festival Energy Science And Technology Ltd filed Critical Anhui Vast Foreign-Festival Energy Science And Technology Ltd
Priority to CN201510302931.1A priority Critical patent/CN104941960A/en
Publication of CN104941960A publication Critical patent/CN104941960A/en
Pending legal-status Critical Current

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Classifications

    • BPERFORMING OPERATIONS; TRANSPORTING
    • B08CLEANING
    • B08BCLEANING IN GENERAL; PREVENTION OF FOULING IN GENERAL
    • B08B7/00Cleaning by methods not provided for in a single other subclass or a single group in this subclass
    • B08B7/0064Cleaning by methods not provided for in a single other subclass or a single group in this subclass by temperature changes
    • B08B7/0071Cleaning by methods not provided for in a single other subclass or a single group in this subclass by temperature changes by heating
    • B08B7/0078Cleaning by methods not provided for in a single other subclass or a single group in this subclass by temperature changes by heating in a fluidized bed

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  • Cleaning In General (AREA)

Abstract

The invention discloses a granular-substance cooling and cleaning fluidized bed, and relates to the technical field of granular-substance cooling and cleaning. The granular-substance cooling and cleaning fluidized bed is characterized in that granular substances enter a fluidized bed surface (6) from a substance inlet (2) and are in contact with air on the bed surface (6), the temperature of the granular substances is adjusted, impurities in the granular substances are removed, the substances obtained after temperature adjustment and cleaning flow out from a substance outlet (3), air enters the granular-substance cooling and cleaning fluidized bed from an air inlet (4) and passes through slant holes in the fluidized bed surface (6) at a certain flowing speed, flowing power is provided for the granular substances passing through the bed surface (6), the air with the impurities and small-granule substances is discharged from an air outlet (5), and the working condition inside a fluidized bed body (1) can be observed from viewing holes (7). By means of the granular-substance cooling cleaning fluidized bed, the aims that the temperature of the granular substances is adjusted to be the required temperature and the impurities in the granular substances and the substances which do not meet the granule specification are removed can be achieved at the same time.

Description

The clean fluid bed of a kind of particulate material cooling
Technical field
The present invention relates to particulate matter cooling clean technologies field, be specifically related to the clean fluid bed of a kind of particulate material cooling.
Background technology
At present, particulate material is had to need cooling reduce temperature and clean at industry, agriculture field.Various way or do not reach the temperature of requirement, or do not reach the cleannes of requirement, or can not accomplish that continuity is run.How meeting the requirement of particulate material temperature with a kind of equipment, meet the requirement of particulate material cleannes, more can meet the requirement run continuously, increase work efficiency, is an important topic to be solved.
Summary of the invention
The object of this invention is to provide the clean fluid bed of a kind of particulate material cooling, particulate material temperature can be adjusted to required temperature by it simultaneously, the foreign material beyond particulate material and the material that do not meet particle size is cleaned out.
In order to solve the problem existing for background technology, the present invention is by the following technical solutions: it comprises fluid bed main body 1, matter inlet 2, material outlet 3, air intlet 4, air outlet slit 5, fluid bed bed surface 6, window 7, particulate material enters into fluid bed bed surface 6 from matter inlet 2, bed surface contacts with air, reach the impurity in the temperature and cleaning particles shape material regulating particulate material, temperature adjustment and the material after cleaning flow out from material outlet 3, air enters from air intlet 4, with certain gas flow rate by the inclined hole on fluid bed bed surface 6, for being provided the power of flowing by the particulate material of bed surface, air containing impurity and finely ground particle substance is got rid of from air outlet slit 5, the working condition inside fluid bed main body 1 can be observed from window 7.
Described fluid bed main body 1 is formed by the steel plate system of enclosing, and the general 5-6mm of steel plate thickness, fixes with stiffener.
Described fluid bed bed surface 6 is positioned at fluid bed main body 1 lower end, and bed surface entrance point is higher than the port of export, and bed surface horizontal sextant angle generally selects 7-10 degree according to particulate material, on fluid bed bed surface 6, rule is covered with 2mm circular hole, circular hole is inclined hole, and incline direction is material outlet direction, and horizontal sextant angle is 60 degree.
Operation principle of the present invention:
Required particulate material to be processed is contacted with air in the space of a sealing, take air as the power run continuously, at particulate material by temperature being adjusted to required temperature during fluid bed, and the foreign material beyond particulate material and the material that do not meet particle size are cleaned out, reach clean object.
Beneficial effect of the present invention:
Particulate material temperature can be adjusted to required temperature by the present invention simultaneously, the foreign material beyond particulate material and the material that do not meet particle size is cleaned out.
Accompanying drawing illustrates:
Fig. 1 is front view of the present invention;
Fig. 2 is top view of the present invention.
(in Fig. 21, matter inlet, 2, material outlet, 3, fluid bed bed surface).
Detailed description of the invention
With reference to Fig. 1, fluid bed main body 1 of the present invention, matter inlet 2, material outlet 3, air intlet 4, air outlet slit 5, fluid bed bed surface 6, window 7, particulate material enters into fluid bed bed surface 6 from matter inlet 2, bed surface contacts with air, reach the impurity in the temperature and cleaning particles shape material regulating particulate material, temperature adjustment and the material after cleaning flow out from material outlet 3, air enters from air intlet 4, with certain gas flow rate by the inclined hole on fluid bed bed surface 6, for being provided the power of flowing by the particulate material of bed surface, air containing impurity and finely ground particle substance is got rid of from air outlet slit 5, the working condition inside fluid bed main body 1 can be observed from window 7.
With reference to Fig. 2, on fluid bed bed surface, rule is covered with 2mm circular hole, and circular hole is inclined hole, and incline direction is material outlet direction, and horizontal sextant angle is 60 degree.

Claims (3)

1. the clean fluid bed of particulate material cooling, it is characterized in that it comprises fluid bed main body (1), matter inlet (2), material outlet (3), air intlet (4), air outlet slit (5), fluid bed bed surface (6), window (7), particulate material enters into fluid bed bed surface (6) from matter inlet (2), bed surface contacts with air, reach the impurity in the temperature and cleaning particles shape material regulating particulate material, temperature adjustment and the material after cleaning flow out from material outlet (3), air enters from air intlet (4), with certain gas flow rate by the inclined hole on fluid bed bed surface (6), for being provided the power of flowing by the particulate material of bed surface, air containing impurity and finely ground particle substance is got rid of from air outlet slit (5), the working condition of fluid bed main body (1) the inside can be observed from window (7).
2. the clean fluid bed of a kind of particulate material cooling according to claim 1, it is characterized in that described fluid bed main body (1) is formed by the steel plate system of enclosing, the general 5-6mm of steel plate thickness, fixes with stiffener.
3. the clean fluid bed of a kind of particulate material cooling according to claim 1, it is characterized in that described fluid bed bed surface (6) is positioned at fluid bed main body (1) lower end, bed surface entrance point is higher than the port of export, bed surface horizontal sextant angle generally selects 7-10 degree according to particulate material, the upper rule of fluid bed bed surface (6) is covered with 2mm circular hole, circular hole is inclined hole, and incline direction is material outlet direction, and horizontal sextant angle is 60 degree.
CN201510302931.1A 2015-06-06 2015-06-06 Granular-substance cooling and cleaning fluidized bed Pending CN104941960A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN201510302931.1A CN104941960A (en) 2015-06-06 2015-06-06 Granular-substance cooling and cleaning fluidized bed

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN201510302931.1A CN104941960A (en) 2015-06-06 2015-06-06 Granular-substance cooling and cleaning fluidized bed

Publications (1)

Publication Number Publication Date
CN104941960A true CN104941960A (en) 2015-09-30

Family

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Family Applications (1)

Application Number Title Priority Date Filing Date
CN201510302931.1A Pending CN104941960A (en) 2015-06-06 2015-06-06 Granular-substance cooling and cleaning fluidized bed

Country Status (1)

Country Link
CN (1) CN104941960A (en)

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN105953606A (en) * 2016-05-23 2016-09-21 肥西县鑫山机械厂 Granular substance cooling and cleaning fluidized bed
CN106123624A (en) * 2016-06-24 2016-11-16 合肥欧克斯新型建材有限公司 A kind of particulate material cooling cleaning fluid bed

Citations (7)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH0445310A (en) * 1990-06-11 1992-02-14 Toray Eng Co Ltd Method for removing organic substance by means of fluidized bed furnace
US6293209B1 (en) * 1997-12-19 2001-09-25 Valtion Teknillinen Tutkimuskeskus Process for treating a material containing metal and organic matter, including metal separation
CN204027369U (en) * 2014-06-23 2014-12-17 安徽瀚洋节能科技有限公司 The clean fluid bed of a kind of particulate material cooling
CN204128325U (en) * 2014-09-18 2015-01-28 常州恒诚富士特干燥设备有限公司 Vibratingfluidbeddrier
CN204177132U (en) * 2014-10-31 2015-02-25 湖南裕华化工集团有限公司 A kind of Vibratingfluidbeddrier
CN204285951U (en) * 2014-11-29 2015-04-22 吴堂军 The fluidized bed dryer that a kind of material not easily coheres
CN104857900A (en) * 2015-06-06 2015-08-26 安徽瀚洋节能科技有限公司 Novel fluidized bed

Patent Citations (7)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH0445310A (en) * 1990-06-11 1992-02-14 Toray Eng Co Ltd Method for removing organic substance by means of fluidized bed furnace
US6293209B1 (en) * 1997-12-19 2001-09-25 Valtion Teknillinen Tutkimuskeskus Process for treating a material containing metal and organic matter, including metal separation
CN204027369U (en) * 2014-06-23 2014-12-17 安徽瀚洋节能科技有限公司 The clean fluid bed of a kind of particulate material cooling
CN204128325U (en) * 2014-09-18 2015-01-28 常州恒诚富士特干燥设备有限公司 Vibratingfluidbeddrier
CN204177132U (en) * 2014-10-31 2015-02-25 湖南裕华化工集团有限公司 A kind of Vibratingfluidbeddrier
CN204285951U (en) * 2014-11-29 2015-04-22 吴堂军 The fluidized bed dryer that a kind of material not easily coheres
CN104857900A (en) * 2015-06-06 2015-08-26 安徽瀚洋节能科技有限公司 Novel fluidized bed

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN105953606A (en) * 2016-05-23 2016-09-21 肥西县鑫山机械厂 Granular substance cooling and cleaning fluidized bed
CN106123624A (en) * 2016-06-24 2016-11-16 合肥欧克斯新型建材有限公司 A kind of particulate material cooling cleaning fluid bed

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Application publication date: 20150930

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