CN110057189B - Integrated preparation kiln and preparation method for inorganic powder and product - Google Patents

Integrated preparation kiln and preparation method for inorganic powder and product Download PDF

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Publication number
CN110057189B
CN110057189B CN201910397346.2A CN201910397346A CN110057189B CN 110057189 B CN110057189 B CN 110057189B CN 201910397346 A CN201910397346 A CN 201910397346A CN 110057189 B CN110057189 B CN 110057189B
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kiln
cover
kiln body
inorganic
inorganic powder
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CN110057189A (en
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赵友谊
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Jingang New Materials Co ltd
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Jingang New Materials Co ltd
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    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F27FURNACES; KILNS; OVENS; RETORTS
    • F27BFURNACES, KILNS, OVENS, OR RETORTS IN GENERAL; OPEN SINTERING OR LIKE APPARATUS
    • F27B7/00Rotary-drum furnaces, i.e. horizontal or slightly inclined
    • F27B7/02Rotary-drum furnaces, i.e. horizontal or slightly inclined of multiple-chamber or multiple-drum type
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F27FURNACES; KILNS; OVENS; RETORTS
    • F27BFURNACES, KILNS, OVENS, OR RETORTS IN GENERAL; OPEN SINTERING OR LIKE APPARATUS
    • F27B7/00Rotary-drum furnaces, i.e. horizontal or slightly inclined
    • F27B7/20Details, accessories, or equipment peculiar to rotary-drum furnaces
    • F27B7/33Arrangement of devices for discharging
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F27FURNACES; KILNS; OVENS; RETORTS
    • F27BFURNACES, KILNS, OVENS, OR RETORTS IN GENERAL; OPEN SINTERING OR LIKE APPARATUS
    • F27B7/00Rotary-drum furnaces, i.e. horizontal or slightly inclined
    • F27B7/20Details, accessories, or equipment peculiar to rotary-drum furnaces
    • F27B7/34Arrangements of heating devices

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  • Engineering & Computer Science (AREA)
  • Mechanical Engineering (AREA)
  • General Engineering & Computer Science (AREA)
  • Muffle Furnaces And Rotary Kilns (AREA)

Abstract

The invention discloses an integrated preparation kiln for inorganic powder and products, which comprises a base, a kiln body, a kiln head cover, a kiln tail cover and a combustion assembly, wherein a discharging cover and an air blast cover are sequentially arranged between the kiln head cover and the kiln tail cover in a sealing manner from left to right on the kiln body. The kiln is characterized in that an air guiding opening is formed in the upper side of the kiln head cover, an air inlet is formed in the air blowing cover, and an air inlet hole is formed in the kiln body and located in the air blowing cover. The kiln body on be located the unloading cover on be provided with a plurality of blanking holes along the circumferencial direction. Meanwhile, an integrated preparation method of inorganic powder and products is also disclosed, and the device and the preparation method can be combined to simultaneously complete the calcination of the inorganic powder and the sintering of the inorganic products, so that energy consumption caused by kiln furniture is not generated, and the thermal efficiency and the sintering speed in the sintering process are improved.

Description

Integrated preparation kiln and preparation method for inorganic powder and product
Technical Field
The invention relates to the technical field of inorganic nonmetallic materials, in particular to an integrated preparation kiln and a preparation method of inorganic powder and products.
Background
In the industry of preparing inorganic powder and products, the calcination of the inorganic powder and the sintering of the inorganic product are carried out independently. The calcination of the inorganic powder is mainly carried out by adopting a rotary kiln, and the sintering of the inorganic product is mainly carried out by adopting a push plate kiln, a tunnel kiln or a roller kiln. When the push plate kiln, the tunnel kiln and the roller kiln are adopted for sintering inorganic products, the prepared inorganic product blank is required to be placed in a special sagger or directly placed on a push plate of the push plate kiln or a roller bed plate of the roller kiln or a kiln car of the tunnel kiln, and then is sent into the kiln for sintering according to the sintering process of the inorganic products. In the process, the sagger, the pushing plate, the backing plate, kiln furniture and other kiln furniture absorb a large amount of heat, the firing time of the products is prolonged, the energy consumption in the firing process of the inorganic products is increased, meanwhile, the fired inorganic products can be taken out from the sagger or other kiln furniture after being cooled, the automation of the firing process is not easy to realize, the production period is long, the production efficiency is low, the working environment of workers is bad, the labor intensity is high, and great potential safety hazards exist.
Disclosure of Invention
In view of the above problems, the present invention provides an integrated preparation kiln for inorganic powder and products, which can simultaneously complete calcination of inorganic powder and sintering of inorganic products, and which does not cause energy consumption due to kiln furniture, and improves thermal efficiency and sintering speed in the sintering process.
Meanwhile, the invention also provides an integrated preparation method of the inorganic powder and the product, which not only improves the production efficiency by fusing the calcination of the inorganic powder and the sintering of the inorganic product, but also effectively wraps the inorganic product in the sintering process, increases the direct heating area of the inorganic product, ensures that the sintering is more sufficient, improves the sintering efficiency, and simultaneously reduces the energy consumption.
The technical scheme adopted for solving the technical problems is as follows:
An integrated preparation kiln for inorganic powder and products comprises a base, a kiln body, a kiln head cover, a kiln tail cover and a combustion assembly, wherein a driving device for driving the kiln body to rotate is arranged between the base and the kiln body, a feed hopper guide groove is arranged on the kiln head cover, a second discharge opening is arranged on the kiln tail cover, and a discharge cover and a blast cover are sequentially arranged on the kiln body from left to right in a sealing manner between the kiln head cover and the kiln tail cover;
an air inlet is formed in the upper side of the kiln head cover, an air inlet is formed in the air blowing cover, and an air inlet hole is formed in the kiln body and located in the air blowing cover;
The kiln body on be located the unloading cover on be provided with a plurality of blanking holes along the circumferencial direction.
Further, the combustion assembly comprises a burner arranged on the kiln tail cover, an extension connecting pipe is arranged on a nozzle of the burner, and a suspension end of the extension connecting pipe penetrates through the blast cover.
Further, the combustion assembly comprises a fuel supply pipe composed of a supply section, a connecting section and a rotating section, wherein the supply section is fixedly arranged on the outer side wall of the kiln body between the kiln head cover and the discharge cover, the rotating section is coaxially arranged with the kiln body and is connected with a fuel supply source through a rotary joint, the supply section and the rotating section are communicated through the connecting section, a plurality of groups of combustors are arranged on the outer side wall of the kiln body between the kiln head cover and the discharge cover, and fuel inlets of the combustors are connected with the supply section through branch pipes.
Further, the burner comprises a burner nozzle, a fuel inlet of the burner nozzle is connected with a supply section of the fuel supply pipe through a branch pipe, and an air inlet of the burner nozzle is connected with the second blower.
Further, burner blocks arranged on the side wall of the kiln body are higher than the inner side wall of the kiln body.
Further, the left end of the rotating section passes through the kiln head cover and then is connected with a fuel supply source through a rotary joint.
Further, the blanking holes are distributed in a certain width area of the kiln body along the axial direction.
Further, a guide hopper is arranged at the upper end of the first discharging opening.
An integrated preparation method of inorganic powder and products comprises the following steps,
Firstly, preparing a green body of an inorganic product by proportioning, pulverizing, shaping and drying;
Secondly, adding raw material powder of inorganic powder and the green body of the inorganic product prepared in the first step into the kiln body according to a certain proportion;
Thirdly, starting the kiln;
fourth, continuously adding the raw material powder of the inorganic powder and the green body of the inorganic product into the feed hopper according to a certain proportion.
The beneficial effects of the invention are as follows:
First, in terms of the device
1. The preparation device can simultaneously complete the calcination of the inorganic powder and the sintering of the inorganic product, realizes the synchronous production of the inorganic powder and the inorganic product in the same kiln, and effectively improves the production efficiency.
2. Aiming at the sintering of inorganic products, the traditional sintering mode of adopting a push plate kiln, a tunnel kiln and a roller kiln is changed, and kiln furniture such as sagger, a backing plate, a push plate, a kiln car and the like are not needed in the sintering process, so that energy consumption caused by using the kiln furniture is avoided, and the thermal efficiency and the sintering speed in the sintering process are improved.
3. The kiln body is provided with the blast cover, and the inorganic products sintered through preliminary cooling can be directly discharged from the second discharge opening, so that the mechanization and automation operation from the feeding of the material into the kiln to the discharging of the sintered products are easy to realize, the problem that the mechanization and automation operation are difficult to realize when the push plate kiln, the tunnel kiln and the roller kiln are used for sintering the inorganic products is solved, and the mechanization and automation level of the sintering process is effectively improved.
Second, in terms of the preparation method
1. According to the method, the calcining of the inorganic powder and the sintering of the inorganic product are combined, so that the processing steps are integrated, and the production efficiency is effectively improved.
2. According to the method, the calcination of the inorganic powder and the sintering of the inorganic product are fused, so that the inorganic powder can effectively wrap the inorganic product in the sintering process, the direct heating area of the inorganic product is increased, the sintering is more sufficient, and the sintering efficiency is improved.
3. According to the method, the calcination of the inorganic powder and the sintering of the inorganic product are fused, so that the inorganic powder can play a role in buffering in the sintering process, the inorganic product is prevented from being cracked and damaged due to mutual collision in the sintering process, and the sintering of the inorganic product in the swing kiln and the rotary kiln is realized.
4. The method fuses the calcination of the inorganic powder and the sintering of the inorganic product, and the inorganic powder and the inorganic product are matched and interacted in the sintering process, so that the method has a good gain effect.
Drawings
FIG. 1 is a front view of a manufacturing apparatus;
FIG. 2 is a schematic view of the internal structure of the manufacturing apparatus;
FIG. 3 is an enlarged schematic view of the portion A in FIG. 2;
FIG. 4 is a schematic view of the overall arrangement of the combustion assembly in the second embodiment;
FIG. 5 is an enlarged schematic view of the portion B of FIG. 4;
FIG. 6 is an enlarged schematic view of the portion C of FIG. 4;
FIG. 7 is a cross-sectional view A-A of FIG. 4;
FIG. 8 is an enlarged schematic view of the portion D in FIG. 7
FIG. 9 is a schematic view showing an arrangement structure of a combustion feed pipe in a second embodiment;
FIG. 10 is a schematic flow chart of an integrated preparation method of inorganic powder and products.
In the figure: the kiln comprises a kiln body, a 11-wheel belt, a 12-blanking hole, a 13-air inlet, a 2-base, a 21-riding wheel, a 31-motor, a 32-speed reducer, a 33-driving wheel, a 34-driven wheel, a 4-kiln hood, a 41-feeding hopper, a 42-guide chute, a 43-air inlet, a 5-discharge hood, a 51-first discharge opening, a 52-guide hopper, a 6-blast hood, a 61-air inlet, a 7-kiln tail hood, a 71-second discharge opening, a 81-burner, a 82-lengthened connecting pipe, a 91-burner, a 92-branch pipe, a 93-second blower, a 94-valve, a 951-supply section, a 952-connecting section, a 953-rotating section and a 96-rotating joint.
Detailed Description
Example 1
As shown in figure 1, an integrated preparation kiln for inorganic powder and products comprises a base 2 and a kiln body 1 rotationally connected with the base 2, wherein a driving device for driving the kiln body 1 to rotate is arranged between the base 2 and the kiln body 1. The kiln body 1 is obliquely arranged in a mode of being high on the left and low on the right or horizontally arranged, and the material axial conveying is realized by using a conveying plate in the kiln body. Preferably, when the kiln body is obliquely arranged, the included angle between the axis of the kiln body 1 and the horizontal plane is 2-8 degrees.
As a specific embodiment, as shown in fig. 1, at least two belts 11 are disposed on the kiln body 1, two supporting wheels 21 for supporting the kiln body 1 are symmetrically disposed below each belt 11 on the base 2, and the belts 11 are pressed on the supporting wheels 21. The driving device comprises a motor 31, a speed reducer 32, a driving wheel 33 and a driven wheel 34. An output shaft of the speed reducer 32 is connected to the driving wheel 33, and a driven wheel 34 engaged with the driving wheel 33 is provided on the kiln body 1.
As shown in figure 1, a kiln head cover 4, a discharging cover 5, a blast cover 6 and a kiln tail cover 7 are sequentially arranged on the kiln body 1 from left to right, and the kiln head cover 4, the discharging cover 5, the blast cover 6 and the kiln tail cover 7 are respectively and hermetically connected with the kiln body 1. The kiln head cover 4, the discharging cover 5, the blast cover 6, the kiln tail cover 7 and the kiln body 1 form a closed space together.
Since in the conventional rotary kiln, a sealing type connection structure exists between the kiln head cover 4, the kiln tail cover 7 and the kiln body 1. Therefore, the sealing structure between the discharging hood 5, the blowing hood 6 and the kiln body 1 only needs to adopt the sealing mechanism between the traditional kiln hood 4, the kiln tail hood 7 and the kiln body 1, which belongs to the prior art and is not described herein.
The kiln is characterized in that a feed hopper 41 is arranged on the outer side face of the kiln head cover 4, a guide chute 42 is arranged on the feed hopper 41, the guide chute 42 is arranged in a downward inclined mode, and the guide chute 42 extends into the kiln body 1.
An air outlet 43 is arranged on the upper side of the kiln head cover 4, and the air outlet 43 is connected with an induced draft fan through a pipeline. The air blowing cover 6 is provided with an air inlet 61, and the air inlet 61 is connected with the first air blower through a pipeline. As shown in fig. 2, an air inlet hole 13 is arranged on the kiln body 1 and positioned in the air blowing cover 6. Preferably, the number of the air inlets 13 is plural, and the air inlets are uniformly distributed along the circumferential direction.
This is mainly set for two reasons: first, during operation, the induced draft fan is induced by the induced draft opening 43, and the air blower blows air through the air inlet 61, so that the air flow in the kiln flows along the axis of the kiln body 1 from right to left, and the air flow and the burner 81 cooperate to realize the control of the temperature field in the kiln. Secondly, when the sintered inorganic product enters the cooling area surrounded by the blast cover 6 from the sintering area of the kiln body 1, the inorganic product can be uniformly cooled by blowing cold air into the kiln body 1. The initially cooled mineral product continues to move to the right along the kiln body 1 axis and finally is discharged through the second discharge opening 71 of the kiln tail hood 7. Is beneficial to realizing mechanical and automatic operation.
As shown in fig. 1 and fig. 2, the discharge cover 5 is provided with a first discharge opening 51, a plurality of blanking holes 12 are formed in the kiln body 1 and located in the discharge cover 5, and the blanking holes 12 are uniformly distributed along the circumferential direction.
Thus, when the calcined inorganic powder and the sintered inorganic product pass through the kiln body 1 surrounded by the discharge hood 5, the inorganic powder enters the discharge hood 5 through the blanking hole 12 on the wall of the kiln body and finally is discharged through the first discharge opening 51 at the lower end of the discharge hood 5, and the sintered inorganic product continues to move rightward along the axis of the kiln body 1.
Further, in order to thoroughly discharge the calcined inorganic powder from the kiln body 1, it is avoided that the inorganic powder is mixed in the finally obtained inorganic product, and as shown in fig. 2, a plurality of rows of blanking holes 12 are axially arranged on the kiln body 1 in the discharge cover 5. As a specific embodiment, 3 rows of blanking holes 12 are axially arranged on the kiln body 1 in the discharging cover 5 in the embodiment.
The blanking holes 12 may not be arranged in rows, and may be arranged in a staggered manner, so long as they are distributed in a certain width region of the kiln body 1 along the axial direction. Preferably, the width of the distribution area is 300-400mm.
Further, in order to facilitate the discharge of the inorganic powder from the first discharge port 51, as shown in fig. 3, a guide hopper 52 is provided at the upper end of the first discharge port 51.
As shown in fig. 1 and 2, the combustion assembly includes a burner 81 disposed on the kiln tail hood 7, and an extension pipe 82 is fixedly disposed on a nozzle of the burner 81, and a suspension end of the extension pipe 82 passes through the blast hood 6, and in this embodiment, the suspension end of the extension pipe 82 extends into the discharge hood 5.
Example two
As shown in fig. 4, the combustion assembly comprises a fuel supply pipe provided on the kiln body 1, and as shown in fig. 6, 7 and 9, the fuel supply pipe comprises a supply section 951, a connection section 952 and a rotation section 953. Wherein the feeding section 951 is fixedly arranged on the outer side wall of the kiln body 1 between the kiln head cover 4 and the discharging cover 5, and the wheel belt 11 and the driven wheel 34 are respectively provided with a through hole for allowing the feeding section 951 to pass through. The rotating section 953 is disposed in the kiln head cover 4 and is coaxially disposed with the kiln body 1. The left end of the rotary segment 953 is connected to a fuel supply through a rotary joint 96 after passing through the kiln head cap 4. The connection section 952 is disposed inside the kiln body 1 and is located on the right side of the guide chute 42, one end of the connection section 952 is connected to the end of the rotation section 953, and the other end of the connection section 952 penetrates through the side wall of the kiln body 1 and then is connected to the end of the supply section 951. Preferably, the connection segments 952 are radially disposed.
The structure of the rotary joint 96 is known in the art and will not be described in detail herein.
As shown in fig. 4, a plurality of groups of burners are axially arranged on the outer side wall of the kiln body 1 between the kiln head cover 4 and the discharge cover 5, and as a specific embodiment, four groups of burners are arranged on the outer side wall of the kiln body 1 in this embodiment. The fuel inlets of the burners are connected to the supply sections 951 of the fuel supply pipes through branch pipes 92, respectively. The nozzles of the burner extend through the side walls of the kiln body 1 to the interior of the kiln body 1.
The branch pipe 92 may be a hose or a hard pipe.
As shown in fig. 5 and 8, the burner includes a burner 91 fixedly disposed on the kiln body 1, a fuel inlet of the burner 91 is connected to a supply section 951 of the fuel supply pipe through a branch pipe 92, and a valve 94 for controlling a fuel flow is disposed on the branch pipe 92. The air inlet of the burner 91 is connected to a second blower 93.
The burner may also be an integrated burner. However, as a preferred embodiment, the burner described in this embodiment adopts a combined structure, mainly because the burner rotates together with the kiln body 1 during operation, so that the smaller the burner volume, the better. If an integrated burner is used, the turning radius is large, and the size of other components needs to be adaptively adjusted according to the size of the burner, for example, the height of the base 2 is increased, which increases the structural size of the whole device.
Further, in order to prevent the burner 91 from being blocked by the inorganic powder or the inorganic product in the kiln body 1 during operation, and to ensure the normal operation of the burner, as shown in fig. 8, the burner block provided on the side wall of the kiln body 1 is higher than the inner side wall of the kiln body 1. The burner block and its mounting structure described herein belong to the prior art and are also applicable to conventional kilns and will not be described in detail herein.
The rest of the structure is the same as that of the first embodiment.
Example III
The rotating section 953 is disposed in the kiln tail cover 7 and is coaxially disposed with the kiln body 1, the right end of the rotating section 953 passes through the kiln tail cover 7 and is connected with a fuel supply source through a rotary joint 96, and the other structures are the same as those of the second embodiment.
An integrated preparation method of inorganic powder and products, as shown in figure 10, comprises the following steps:
firstly, preparing materials, pulverizing, forming and drying to obtain a green body of the inorganic product.
Secondly, adding the raw material powder of the inorganic powder and the green body of the inorganic product prepared in the first step into the kiln body 1 according to a certain proportion.
Here, the ratio of the raw material powder of the inorganic powder to the green body of the inorganic product varies depending on the kind of the inorganic product.
Thirdly, starting the kiln.
Fourth, raw material powder of inorganic powder and a green body of inorganic product are continuously added into the hopper 41 in a certain ratio.
Here, the ratio of the raw material powder of the inorganic powder to the green body of the inorganic product varies depending on the kind of the inorganic product.
The raw material powder of the inorganic powder is not only the raw material required by the firing of the inorganic powder, but also the buffer and lubricant between the inorganic products and the kiln body 1.

Claims (5)

1. An integrated preparation method of inorganic powder and products is applied to an integrated preparation kiln of inorganic powder and products, and is characterized in that: the kiln comprises a base, a kiln body, a kiln head cover, a kiln tail cover and a combustion assembly, wherein a driving device for driving the kiln body to rotate is arranged between the base and the kiln body, a feed hopper guide groove is arranged on the kiln head cover, a second discharge opening is arranged on the kiln tail cover, and a discharge cover and an air blast cover are sequentially arranged on the kiln body from left to right in a sealing manner between the kiln head cover and the kiln tail cover;
an air inlet is formed in the upper side of the kiln head cover, an air inlet is formed in the air blowing cover, and an air inlet hole is formed in the kiln body and located in the air blowing cover;
The kiln body is provided with a first discharging opening, and a plurality of blanking holes are formed in the discharging cover along the circumferential direction;
the combustion assembly comprises a fuel supply pipe composed of a supply section, a connecting section and a rotating section, wherein the supply section is fixedly arranged on the outer side wall of the kiln body between the kiln head cover and the discharge cover, the rotating section is coaxially arranged with the kiln body, the left end of the rotating section passes through the kiln head cover and then is connected with a fuel supply source through a rotating joint, the supply section and the rotating section are communicated through the connecting section, a plurality of groups of burners are arranged on the outer side wall of the kiln body between the kiln head cover and the discharge cover, each burner comprises a burner, a fuel inlet of each burner is connected with the supply section of the fuel supply pipe through a branch pipe, an air inlet of each burner is connected with a second air blower, and the burner of each burner extends to the inside of the kiln body through the side wall of the kiln body;
the kiln comprises a kiln head cover, and is characterized in that a feed hopper is arranged on the outer side surface of the kiln head cover, a guide chute is arranged on the feed hopper, the guide chute is arranged in a downward inclined mode, and the guide chute extends into the kiln body;
The driving device comprises a motor, a speed reducer, a driving wheel and a driven wheel, an output shaft of the speed reducer is connected with the driving wheel, the driven wheel meshed with the driving wheel is arranged on the kiln body, a wheel belt is arranged on the kiln body, and through holes allowing the feeding section to pass through are formed in the wheel belt and the driven wheel;
the connecting section is arranged in the kiln body and is positioned on the right side of the guide chute, one end of the connecting section is connected with the end part of the rotating section, and the other end of the connecting section penetrates through the side wall of the kiln body and then is connected with the end part of the feeding section;
the integrated preparation method of the inorganic powder and the product comprises the following steps,
Firstly, preparing a green body of an inorganic product by proportioning, pulverizing, shaping and drying;
Secondly, adding raw material powder of inorganic powder and the green body of the inorganic product prepared in the first step into the kiln body according to a certain proportion;
Thirdly, starting the kiln;
Fourth, the raw material powder of the inorganic powder and the green body of the inorganic product are continuously added into the feed hopper according to a certain proportion, when the calcined inorganic powder and the inorganic product pass through the kiln body surrounded by the discharge cover, the inorganic powder enters the discharge cover through the blanking hole on the wall of the kiln body and finally is discharged through the first discharge opening at the lower end of the discharge cover, the calcined inorganic product continues to move rightwards along the axis of the kiln body, when the calcined inorganic product enters the cooling area surrounded by the blast cover from the sintering area of the kiln body, the inorganic product is uniformly cooled by blowing cold air into the kiln body, the cooled inorganic product continues to move rightwards along the axis of the kiln body, and finally is discharged through the second discharge opening of the kiln tail cover.
2. The integrated production method of an inorganic powder and a product according to claim 1, characterized in that: the combustion assembly comprises a burner arranged on the kiln tail cover, and a lengthening connecting pipe is arranged on a burner nozzle of the burner and penetrates through the blast cover.
3. The integrated production method of an inorganic powder and a product according to claim 1, characterized in that: the burner blocks arranged on the side wall of the kiln body are higher than the inner side wall of the kiln body.
4. The integrated production method of an inorganic powder and a product according to claim 1, characterized in that: the blanking holes are distributed in a certain width area of the kiln body along the axial direction.
5. The integrated production method of an inorganic powder and a product according to claim 1, characterized in that: the upper end of the first discharging opening is provided with a guide hopper.
CN201910397346.2A 2019-05-14 2019-05-14 Integrated preparation kiln and preparation method for inorganic powder and product Active CN110057189B (en)

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CN110057189B true CN110057189B (en) 2024-04-19

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Families Citing this family (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN114322536B (en) * 2020-09-30 2023-11-03 江苏鑫浩新材料科技有限公司 Belt type ceramsite sintering machine and belt type ceramsite sintering method

Citations (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US3881862A (en) * 1972-09-04 1975-05-06 Kawasaki Heavy Ind Ltd Apparatus for calcination of cement-clinker
CN1137786A (en) * 1994-09-08 1996-12-11 川崎重工业株式会社 Method and apparatus for making cement clinker by firing
CN106679366A (en) * 2017-03-07 2017-05-17 唐竹胜 Roller type drying and sintering or roasting device
CN208124854U (en) * 2018-04-20 2018-11-20 唐竹胜 A kind of huge two-sided rotary heating rotary kiln device of muffle
CN109179468A (en) * 2018-09-17 2019-01-11 石嘴山市鹏盛化工有限公司 The raw materials for production and its production technology of ash production calcium oxide are purified using calcium carbide furnace gas
CN209926834U (en) * 2019-05-14 2020-01-10 金刚新材料股份有限公司 Integrated preparation furnace kiln for inorganic powder and products

Patent Citations (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US3881862A (en) * 1972-09-04 1975-05-06 Kawasaki Heavy Ind Ltd Apparatus for calcination of cement-clinker
CN1137786A (en) * 1994-09-08 1996-12-11 川崎重工业株式会社 Method and apparatus for making cement clinker by firing
CN106679366A (en) * 2017-03-07 2017-05-17 唐竹胜 Roller type drying and sintering or roasting device
CN208124854U (en) * 2018-04-20 2018-11-20 唐竹胜 A kind of huge two-sided rotary heating rotary kiln device of muffle
CN109179468A (en) * 2018-09-17 2019-01-11 石嘴山市鹏盛化工有限公司 The raw materials for production and its production technology of ash production calcium oxide are purified using calcium carbide furnace gas
CN209926834U (en) * 2019-05-14 2020-01-10 金刚新材料股份有限公司 Integrated preparation furnace kiln for inorganic powder and products

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