CN201043159Y - Controlled released large grain seed-coating machine - Google Patents

Controlled released large grain seed-coating machine Download PDF

Info

Publication number
CN201043159Y
CN201043159Y CNU2007200334046U CN200720033404U CN201043159Y CN 201043159 Y CN201043159 Y CN 201043159Y CN U2007200334046 U CNU2007200334046 U CN U2007200334046U CN 200720033404 U CN200720033404 U CN 200720033404U CN 201043159 Y CN201043159 Y CN 201043159Y
Authority
CN
China
Prior art keywords
coating
guide cylinder
dressing
tower
lower cone
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.)
Expired - Lifetime
Application number
CNU2007200334046U
Other languages
Chinese (zh)
Inventor
查国才
查文龙
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.)
Individual
Original Assignee
Individual
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 Individual filed Critical Individual
Priority to CNU2007200334046U priority Critical patent/CN201043159Y/en
Application granted granted Critical
Publication of CN201043159Y publication Critical patent/CN201043159Y/en
Anticipated expiration legal-status Critical
Expired - Lifetime legal-status Critical Current

Links

Images

Landscapes

  • Nozzles (AREA)

Abstract

The utility model relates to a facility used for coating and drying granular material in the fields of pharmacy, chemical industry, food and agriculture, in particular to a sustained and controlled release large grain coating machine used for coating and drying large granular materials. The utility model consists of a steam heater, a main engine, a feeding device, a cyclone separator, a condensing plant and a blower, which are connected one by one to form an enclosed loop. A coating liquid outlet is arranged at the bottom of the condensing plant. A discharge opening is arranged at the bottom of the main engine. The utility model overcomes the defects of prior coating facility that the large granular material can not be coated and the coating liquid of opening coating facility can not be recycled, which not only results in the waste of the coating liquid, but also adds coating cost and pollutes the environment. The utility model solves the coating problem of the large granular material, the diameter of which is more than 3mm, with a good coating effect. A layer of compact coating membrane is formed on the surface of the large granular material. Furthermore, the coating liquid can be recycled, which can save the coating liquid, reduce coating cost and does not pollute the environment.

Description

Slow control large grained lagging cover machine
Technical field
The utility model relates to the equipment of the granule materials dressing drying process in fields such as pharmacy, chemical industry, food, agricultural, particularly large granular materials is carried out dressing exsiccant slow control large grained lagging cover machine.
Background technology
During common dressing equipment design general wind speed all<4m/s, coating effect to some molecules such as medicines is more satisfactory, and large granular materials is carried out dressing, often can not form fluidization, and when dressing, can not form good material endless chain, coating liquid just can not atomize uniformly on the material surface, does not also just form the coating membrance of one deck densification on the material surface, and the final material that forms does not just have the effect of slowly-releasing, controlled release yet.And also just can not dressing for the macrobeads such as slow controlled-release compound fertilizer of picture in the fertilizer industry, do not improve fertilizer utilization ratio.
Secondly traditional fluidization dressing equipment all is open type, and the coating liquid that contains organic solvent that uses in the dressing operation all can not recycle, and has not only caused the coating liquid waste, has increased the dressing cost virtually, and has polluted the environment.
Summary of the invention
The technical problems to be solved in the utility model is: overcoming existing dressing equipment can not carry out dressing to large granular materials; The coating liquid of the dressing equipment of open type can not recycle, not only cause the coating liquid waste, increase the dressing cost, and the deficiency that pollutes the environment, the utility model provides a kind of slow control large grained lagging cover machine, solved the dressing problem of diameter, and coating effect is good, can forms the coating membrance of one deck densification on the large granular materials surface greater than the large granular materials of 3mm; Coating liquid can recycle in addition, has saved coating liquid, has reduced the dressing cost, does not pollute the environment.
The technical scheme that its technical problem that solves the utility model adopts is: a kind of slow control large grained lagging cover machine, has the steam heater that connects successively, main frame, feeding unit, cyclonic separator and condensing equipment, be provided with the spray gun of spray coating liquid in the main frame, the blast inlet of cyclonic separator is connected with feeding unit bottom and dressing tower top, the air outlet of cyclonic separator links to each other with the blast inlet of condensing equipment by pipeline, the air outlet of condensing equipment be connected with blower fan by pipeline, the air outlet of blower fan is connected with the blast inlet of steam heater by pipeline, the bottom of condensing equipment is provided with the coating liquid outlet, and the bottom of main frame is provided with discharge port.Coating liquid is pressed into spray gun by infusion pump; spray by spray gun; atomizing is on the material surface; and constantly being blown into along with hot blast; the wet air that contains organic solvent is along with hot blast enters into condensing equipment; and organic solvent is collected recycle and reuse again after by the condensing equipment condensation, has so just saved the dressing cost, has protected environment simultaneously.Tradition dressing drying plant when dressing just begins because the minute quantity fine powder that collision produces all is to collect by sack cleaner, dust then adopts cyclonic separator to collect in the utility model, be collected in than traditional sack cleaner like this and reduced 1000Pa on the systemic resistance, and changed in traditional packaging technique cloth bag and very easily bondd and influence permeability by coating liquid, so both reduce systemic resistance, saved fan energy consumption again.
For improving the organic solvent rate of recovery, the described condensing equipment condenser group that at least two condensers are in series of serving as reasons, the air outlet of cyclonic separator links to each other by the blast inlet of pipeline with the chopped-off head condenser, the air outlet of backing condenser links to each other by the blast inlet of pipeline with back level condenser, and the air outlet of last condenser stage is connected with blower fan by pipeline.
Described main frame has the dressing tower, the dressing tower is made up of the cylinder body of the tower and the lower cone that fuse, be provided with guide cylinder in the lower cone of dressing tower, also be equipped with on the lower cone and be used for the guide cylinder lifting device of lifting guide cylinder, the height of dressing tower compares more than or equal to 4 with the diameter of cylinder body of the tower, feeding unit feeds dressing tower inner chamber at dressing tower middle part, spray gun be arranged on the guide cylinder center under, the hydrojet direction of spray gun is for vertically upward.The height of dressing tower compares more than or equal to 4 with the diameter of cylinder body of the tower, guide cylinder is set in lower cone, pass through to satisfy most of air quantity, when wind speed greater than 20m/s, macrobead can form the fluidization of class fountain type, particle is quickened by air-flow in the guide cylinder and rises, leave guide cylinder again from the center ejection, to around be scattering into annular zone, rely on self gravitation slowly to descend then, sprayed by upstream again to awl at the end and gone, so circulation, the hydrojet direction of spray gun is consistent with particle motion, and the spray gun hydrojet is quick, continue, homogeneous, coating liquid are sprayed near the orderly particle surface of the motion of nozzle, drop is to shorter by bag particle surface distance, easily form continuously coating membrance closely, thereby make the dressing yield rate of material reach nearly 100%, more satisfactory to the particle effect of coating diameter>3mm.
For making the guide cylinder position adjustments convenient, described guide cylinder lifting device has axle, axle is located in the lower cone middle part, be set with gear on the axle, the guide cylinder outer wall is fixed with tooth bar along the guide cylinder axis, the wheel and rack engagement, be fixed with bearing support on the lower cone outer wall at axle two ends, is connected by bearing between axle and bearing support, the bearing support outside spool on be set with ratchet-wheel gear and handwheel, the lower cone internal fixing has guide ring, guide ring is made up of interior ring and gib block, gib block one end is fixedlyed connected with the lower cone inwall, the other end is fixedlyed connected with interior ring, and guide cylinder is slidingly connected by feather key and interior ring, and described guide ring has more than two or two.
The beneficial effects of the utility model are, the height of slow control large grained lagging cover machine dressing tower of the present utility model compares more than or equal to 4 with the diameter of cylinder body of the tower, guide cylinder is set in lower cone, pass through to satisfy most of air quantity, when wind speed greater than 20m/s, macrobead can form the fluidization of class fountain type, the hydrojet direction of spray gun is consistent with particle motion, hydrojet in the same way, hydrojet is quick, continue, homogeneous, coating liquid is sprayed near the orderly particle surface of the motion of nozzle, drop easily forms continuously coating membrance closely, thereby makes the dressing yield rate of material reach nearly 100% to shorter by bag particle surface distance, particle effect to coating diameter>3mm is more satisfactory, and the coating membrance quality is good, be suitable for macrobead and production in enormous quantities.
Description of drawings
Below in conjunction with drawings and Examples the utility model is further specified.
Fig. 1 is a structural representation of the present utility model.
Fig. 2 is the structural representation of the guide cylinder lifting device in the utility model.
Fig. 3 is the vertical view of Fig. 2.
Fig. 4 is the left view of Fig. 2.
Fig. 5 is the I partial enlarged drawing of Fig. 2.
Fig. 6 is the II partial enlarged drawing of Fig. 2.
Fig. 7 is that the A of Fig. 2 is to view.
1. steam heaters among the figure, 2. main frame, 21. discharge ports, 22. the dressing tower, 221. cylinder bodies of the tower, 222. lower cones, 3. feeding unit, 4. blower fan, 5. spray gun, 6. condensing equipment, the outlet of 61. coating liquids, 7. cyclonic separator, 8. guide cylinder, 9. guide cylinder lifting device, 91., 92. gear, 93. tooth bars, 94. bearing supports, 95. ratchet-wheel gear, 96. handwheels, 97. guide rings, 971. interior ring, 972. gib blocks, 98. feather keys, 100. fertilizer, 101. fine powders, 102. coating liquids, 103. the water coolant trend, 104. air directs, 105. materials trend.
Embodiment
Slow control large grained lagging cover machine of the present utility model shown in Fig. 1~7, has the steam heater 1 that connects successively, main frame 2, feeding unit 3, cyclonic separator 7, condensing equipment 6 and blower fan 4, the condenser group of condensing equipment 6 for being in series by three condensers, be provided with the spray gun 5 of spray coating liquid 102 in the main frame 2, the bottom of main frame 2 is provided with discharge port 21, main frame 2 has dressing tower 22, dressing tower 22 is made up of cylinder body of the tower 221 that fuses and lower cone 222, be provided with guide cylinder 8 in the lower cone 222 of dressing tower 22, also be equipped with on the lower cone 222 and be used for the guide cylinder lifting device 9 of lifting guide cylinder 8, guide cylinder lifting device 9 has axle 91, axle 91 is located in lower cone 222 middle parts, be set with gear 92 on the axle 91, guide cylinder 8 outer walls are fixed with tooth bar 93 along the guide cylinder axis, gear 92 and tooth bar 93 engagements, be fixed with bearing support 94 on lower cone 222 outer walls at axle 91 two ends, axle 91 is connected by bearing with 94 of bearing supports, on the axle 91 in a bearing support 94 outsides, be set with ratchet-wheel gear 95 and handwheel 96, on lower cone 222 internal fixing have, following two guide rings 97, guide ring 97 is made up of interior ring 971 and gib block 972, gib block 972 1 ends are fixedlyed connected with lower cone 222 inwalls, the other end is fixedlyed connected with interior ring 971, guide cylinder 8 is slidingly connected by feather key 98 and interior ring 971, the height of dressing tower 22 compares more than or equal to 4 with the diameter of cylinder body of the tower 221, feeding unit 3 communicates with dressing tower 22 inner chambers at dressing tower 22 middle parts, spray gun 5 be arranged on guide cylinder 8 centers under, the hydrojet direction of spray gun 5 is for vertically upward, the blast inlet of cyclonic separator 7 is connected with feeding unit 3 bottoms and dressing tower 22 tops, the air outlet of cyclonic separator 7 links to each other with the blast inlet of first-stage condenser by pipeline, the air outlet of first-stage condenser links to each other with the blast inlet of secondary condenser by pipeline, the air outlet of secondary condenser links to each other by the blast inlet of pipeline with three grades of condensers, the air outlet of three grades of condensers is connected with blower fan 4 by pipeline, the air outlet of blower fan 4 is connected first-stage condenser by the blast inlet of pipeline with steam heater 1, the bottom of secondary condenser and three grades of condensers is provided with coating liquid outlet 61.
During work, will coated granules add in the dressing tower 22 and in the outside of guide cylinder 8 by feeding unit 3; Start blower fan 4; Open steam heater 1, air is heated, make temperature reach required requirement; Blower fan 4 can be connected with a frequency transformer, by frequency transformer air quantity is regulated, and makes air quantity reach required requirement; Regulate the height of guide cylinder 8, granular material is outflowed in guide cylinder 8 from guide cylinder 8, the materials in the guide cylinder 8 are upwards sprayed material by the high velocity air that blower fan 4 produces, and material spilling forms a circulation outside guide cylinder 8; Coating liquid 102 is pressed into spray gun 5 by infusion pump, by spray gun 5 ejections, material is carried out dressing, regulates air supply and spouting liquid simultaneously, and the material spray dressing liquid in the spray gun 5 alignment guide tubes 8 is at the coating membrance of granular material surface formation one deck densification; Open the low-temperature receiver of condensing equipment 6, the solvent in the coating liquid 102 is reclaimed; Moisture is constantly discharged in the dressing process, and fresh air constantly replenishes, wait coating liquid 102 spray after, drying for some time steam off well heater 1, blower fan 4 are opened discharge port 21 material are unloaded to going out trolley.The macrobeads such as slow controlled-release compound fertilizer that the utility model can be used in the fertilizer industry carry out dressing, make granular material obtain slow-releasing and controlled-releasing action, improve the utilization ratio of fertilizer 100.

Claims (5)

1. slow control large grained lagging cover machine, has steam heater (1), main frame (2), feeding unit (3) and blower fan (4), steam heater (1), main frame (2) and feeding unit (3) connect successively, be provided with the spray gun (5) of spray coating liquid in the main frame (2), it is characterized in that: also have condensing equipment (6) and cyclonic separator (7), the blast inlet of cyclonic separator (7) is connected with feeding unit (3) bottom and main frame (2) top, the air outlet of cyclonic separator (7) links to each other by the blast inlet of pipeline with condensing equipment (6), the air outlet of condensing equipment (6) be connected with blower fan (4) blast inlet by pipeline, the air outlet of blower fan (4) is connected by the blast inlet of pipeline with steam heater (1), the bottom of condensing equipment (6) is provided with coating liquid outlet (61), and the bottom of main frame (2) is provided with discharge port (21).
2. slow control large grained lagging cover machine according to claim 1, it is characterized in that: described condensing equipment (6) the condenser group that at least two condensers are in series of serving as reasons, the air outlet of cyclonic separator (7) links to each other by the blast inlet of pipeline with the chopped-off head condenser, the air outlet of backing condenser links to each other by the blast inlet of pipeline with back level condenser, and the air outlet of last condenser stage is connected with blower fan (4) blast inlet by pipeline.
3. slow control large grained lagging cover machine according to claim 1, it is characterized in that: described main frame (2) has dressing tower (22), dressing tower (22) is made up of cylinder body of the tower (221) that fuses and lower cone (222), be provided with guide cylinder (8) in the lower cone (222) of dressing tower (22), also be equipped with on the lower cone (222) and be used for the guide cylinder lifting device (9) of lifting guide cylinder (8), the ratio of the diameter D of the height H of dressing tower (22) and cylinder body of the tower (221) is more than or equal to 4, feeding unit (3) communicates with dressing tower (22) inner chamber at dressing tower (22) middle part, spray gun (5) be arranged on guide cylinder (8) center under, the hydrojet direction of spray gun (5) is for vertically upward.
4. slow control large grained lagging cover machine according to claim 3, it is characterized in that: described guide cylinder lifting device (9) has axle (91), axle (91) is located in lower cone (222) middle part, be set with gear (92) on the axle (91), guide cylinder (8) outer wall is fixed with tooth bar (93) along the guide cylinder axis, gear (92) and tooth bar (93) engagement, be fixed with bearing support (94) on lower cone (222) outer wall at axle (91) two ends, be connected by bearing between axle (91) and bearing support (94), on the axle (91) in a bearing support (94) outside, be set with ratchet-wheel gear (95) and handwheel (96), lower cone (222) internal fixing has guide ring (97), guide ring (97) is made up of interior ring (971) and gib block (972), gib block (972) one ends are fixedlyed connected with lower cone (222) inwall, the other end is fixedlyed connected with interior ring (971), and guide cylinder (8) is slidingly connected by feather key (98) and interior ring (971).
5. slow control large grained lagging cover machine according to claim 4 is characterized in that: described guide ring (97) has more than two or two.
CNU2007200334046U 2007-01-05 2007-01-05 Controlled released large grain seed-coating machine Expired - Lifetime CN201043159Y (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CNU2007200334046U CN201043159Y (en) 2007-01-05 2007-01-05 Controlled released large grain seed-coating machine

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CNU2007200334046U CN201043159Y (en) 2007-01-05 2007-01-05 Controlled released large grain seed-coating machine

Publications (1)

Publication Number Publication Date
CN201043159Y true CN201043159Y (en) 2008-04-02

Family

ID=39258051

Family Applications (1)

Application Number Title Priority Date Filing Date
CNU2007200334046U Expired - Lifetime CN201043159Y (en) 2007-01-05 2007-01-05 Controlled released large grain seed-coating machine

Country Status (1)

Country Link
CN (1) CN201043159Y (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN102134173A (en) * 2011-04-26 2011-07-27 中国科学院南京土壤研究所 Method for manufacturing slow control release fertilizer on the basis of a coating machine of a closed type fluidized bed and equipment thereof

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN102134173A (en) * 2011-04-26 2011-07-27 中国科学院南京土壤研究所 Method for manufacturing slow control release fertilizer on the basis of a coating machine of a closed type fluidized bed and equipment thereof

Similar Documents

Publication Publication Date Title
US20240042480A1 (en) Fluid Bed Granulation Process and Apparatus
US2561392A (en) Process and apparatus for treating solutions to recover and coat solid particles
CN100556524C (en) Gravitational method continuous granulator and prilling process
CN100537013C (en) Large-granule coating machine
CN101949635B (en) Closed cycle spray drying and solvent recovery system
CN1331587C (en) Circular spout bed equipped with circular multi-nozzle ventilation mechanism
CN201926251U (en) Closed cycle spray-drying and solvent-recovery device
CN1551797B (en) Fluid bed granulation process
CN203342748U (en) Granulating and drying device of vertical continuous fluidized bed
CN101274243A (en) Technique for producing grain with one-step method containing atomization, fluidization, granulation and dessication
CN201043159Y (en) Controlled released large grain seed-coating machine
CN1298681C (en) Continuous production device of slow-release or control-release fertilizer
CN201042662Y (en) Controlled released large grain seed-coating machine
CN202270504U (en) Multifunctional pelleting device of fluidized bed
CN110370490A (en) A kind of pre-crystallized technique of PTT continuous polymerization
CN203971871U (en) The granulating coated device of a kind of effective fluidized bed
CN102847486A (en) Spray granulation fluidized drying system
CN205216230U (en) Drying tower with dual drying function
CN101091892A (en) Horizontal continuous granulating apparatus of using gravity method
CN113318662A (en) Calcium carbonate powder activation processing device
CN202554958U (en) Horizontal fluidized bed
US3475195A (en) Process and apparatus for granulating paste
CN201042661Y (en) Gravitational method horizontal continuous granulation equipment
CN101132850A (en) Process and device for fluidized bed granulation
CN2629820Y (en) Fluidized bed spray granulating machine

Legal Events

Date Code Title Description
C14 Grant of patent or utility model
GR01 Patent grant
EE01 Entry into force of recordation of patent licensing contract

Assignee: Changzhou Yibu Drying Equipment Co., Ltd.

Assignor: Cha Guocai

Contract fulfillment period: 2008.4.20 to 2016.4.19

Contract record no.: 2009320000733

Denomination of utility model: Controlled released large grain seed-coating machine

Granted publication date: 20080402

License type: Exclusive license

Record date: 20090504

LIC Patent licence contract for exploitation submitted for record

Free format text: EXCLUSIVE LICENSE; TIME LIMIT OF IMPLEMENTING CONTACT: 2008.4.20 TO 2016.4.19; CHANGE OF CONTRACT

Name of requester: CHANGZHOU ONE-STEP DRYING EQUIPMENT CO., LTD.

Effective date: 20090504

CX01 Expiry of patent term

Granted publication date: 20080402

EXPY Termination of patent right or utility model