CN2475979Y - Lauryl alcohol (foaming agent) spraying-drying cooling tower - Google Patents
Lauryl alcohol (foaming agent) spraying-drying cooling tower Download PDFInfo
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- CN2475979Y CN2475979Y CN 01218063 CN01218063U CN2475979Y CN 2475979 Y CN2475979 Y CN 2475979Y CN 01218063 CN01218063 CN 01218063 CN 01218063 U CN01218063 U CN 01218063U CN 2475979 Y CN2475979 Y CN 2475979Y
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- cyclone separator
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Abstract
The utility model provides a spray drying cooling tower for dodecanol (a foaming agent), comprising a main tower, a central air intake chamber, a first air intake chamber, a second air intake chamber, a first air averaging plate arranged with a spray gun, a second air averaging plate, a cyclone separator, an annular air duct, a cooling sleeve, an induced draft fan, an unloader, a product cooling pipe, a first cyclone separator, a first induced draft fan, and a second induced draft fan. The utility model can effectively overcome the thermosensitive problems of the liquid material produced during the drying process, meanwhile, the requirement that the moisture content in the finished solid material must less than 5 percent and the requirement of the white color are achieved, the utility model provides the guarantee to the equipment for industrialized production, which has a good social and economic benefit.
Description
The utility model relates to chemical industry thermal sensitivity liquid material drying device field, particularly relates to a kind of dry cooling tower of blowing agent liquid material.
Raising along with China's resident living level, people are when material life improves, living environment is beautified, the raising of quality of life has had new requirement, so that to urban environmental hygiene, public place and resident living articles for use, the washing agent that cleaners and polishes are required, the use amount of disinfectant and cleaning agent increases day by day, and the primary raw material lauryl alcohol (blowing agent) of goods such as above-mentioned washing agent is a chemical industry thermal sensitivity liquid material, as be directly used in industrialization production, bring difficulty not only for the preparing process in producing, and the storage of liquid towards material, transportation all causes difficulty in various degree, for this processes the liquid material of lauryl alcohol (blowing agent), to be not more than 5% solid-state material be the key that solves above-mentioned difficulties to reach its water content.
Yet lauryl alcohol (blowing agent) is because chemical industry thermal sensitivity characteristics, and promptly the solid material thawing will occur when temperature reaches 70 when spending, bring difficulty for again the drying processing of this liquid state material, if adopt low temperature drying, its production efficiency is lower for this reason, production cost height, economic benefit are not good.
The purpose of this utility model is lauryl alcohol (blowing agent) the spray-drying cooling tower that a kind of can efficient drying liquid heat sensitive material to water content of design is lower than 5% solid material.
The technical solution of the utility model is as follows: lauryl alcohol (blowing agent) spray-drying cooling tower, has a king-tower, the king-tower top be provided with one with add the central inlet air plenum that warm-air pipe connects, inlet air plenum that at least one communicates with central inlet air plenum by pipeline and at least one with add the secondary air chamber that warm-air pipe connects, the lower end air outlet of central authorities' inlet air plenum in king-tower is provided with homogenating plate one time, the lower end air outlet of an inlet air plenum in king-tower is provided with spray gun, the lower end air outlet of secondary air chamber in king-tower is provided with the secondary homogenating plate, spray gun connects feed voltage-stablizer and high-pressure delivery pump successively by feeder sleeve, tower body middle part arranged outside has with the lower end and has the air loop duct that medial surface that the cyclone separator of blanking device communicates has two little gas air inlets at least, the tower body below is the reverse taper coolant jacket, the upper opening of coolant jacket is equipped with air-introduced machine, the bottom is provided with wind stopping device, wind stopping device, the lower end of blanking device communicates with the finished product cooling tube that an end is provided with air cleaner, the other end of finished product cooling tube and lower end are that a cyclone separator of feed bin communicates, and the top of cyclone separator is by an air-introduced machine, the top of a cyclone separator communicates with wet exhauster by pipeline respectively by the secondary air-introduced machine.
According to the further technical measures of aforementioned schemes, also be provided with a deduster between a described cyclone separator and secondary air-introduced machine, the below of deduster is provided with a collector that has baiting valve.
According to the further technical measures of aforementioned schemes, the madial wall of described king-tower, coolant jacket, dedusting, feed bin is provided with vibrator.
Further again technical measures according to aforementioned schemes are provided with blanking device one time between a described cyclone separator and feed bin, and the feed bin below is provided with baiting valve.
According to the further again technical measures of aforementioned schemes, deduster and feed bin top are provided with compressed air hose.
The utility model using liquid high temperature (about 300 degree) wink-dry and dried wet feed low temperature neutralization (about 35 degree) drying and finished product be the technological principle of cooling indirectly, can overcome the thermal sensitivity difficult problem that this liquid material produces effectively in drying, the water content that reaches finished product solid material simultaneously reaches white color and luster requirement below 5%, for providing equipment, industrialization production guarantees to have good society, economic benefit.
Below in conjunction with description of drawings embodiment of the present utility model:
Fig. 1 is the structural representation of embodiment;
Fig. 2 is the A-A cutaway view of Fig. 1;
Fig. 3 is the vertical view of king-tower among Fig. 1; Fig. 4 is the B-B cutaway view of Fig. 3:
Fig. 5 is for once dividing equally the plate schematic diagram;
Fig. 6 divides equally the plate schematic diagram for secondary.
King-tower 1 top be provided with one with add the central inlet air plenum 2 that warm-air pipe connects, three inlet air plenum 3 passing through that pipeline communicates with central inlet air plenum 2 that are distributed on cat head and three are distributed on cat head and add the secondary air chamber 4 that warm-air pipe connects, the lower end air outlet of central authorities' inlet air plenum 2 in king-tower 1 is provided with a homogenating plate 5 of grid palisade, the lower end air outlet of an inlet air plenum 3 in king-tower 1 is provided with spray gun 31, the lower end air outlet of secondary air chamber 4 in king-tower 1 is provided with and has the secondary homogenating plate 41 of dividing equally hole 411, spray gun 31 connects feed voltage-stablizer 33 and high-pressure delivery pump 34 successively by feeder sleeve 32, tower body middle part arranged outside has with the lower end and has the air loop duct 7 that medial surface that the cyclone separator 6 of blanking device 61 communicates has four uniform little gas air inlets 71, the tower body below is a reverse taper coolant jacket 8, the upper opening of coolant jacket 8 is equipped with air-introduced machine 9, the bottom is provided with wind stopping device 81, wind stopping device 81, the lower end of blanking device 61 communicates with the finished product cooling tube 10 that an end is provided with air cleaner 101, the other end of finished product cooling tube 10 and lower end are that a cyclone separator 11 of feed bin 111 communicates, cyclone separator 11 and 111 of feed bins are provided with blanking device 112 one time, feed bin 111 belows are provided with baiting valve 17, and feed bin 111 tops are provided with compressed air hose 16.The top of cyclone separator 6 communicates with wet exhauster 14 by pipeline by an air-introduced machine 12.13 of cyclone separator 11 and secondary air-introduced machines are connected with a deduster 15 by pipeline, and the below of deduster 15 is provided with a collector 151 that has baiting valve 17, and the top of deduster 15 is provided with compressed air hose 16.The top of deduster 15 communicates with wet exhauster 14 by pipeline by secondary air-introduced machine 13.King-tower 1, coolant jacket 8, madial wall be provided with vibrator 82.
For ease of understanding present embodiment, below the summary present embodiment the course of work: by external add the warm-air pipe hot-air from central inlet air plenum enter be preheated in the king-tower 80 the degree, kept 12 hours, be heated to 300 degree gradually, the while high-pressure delivery pump is delivered to spray gun with liquid material (liquid lauryl alcohol blowing agent) and is atomized, start the secondary air chamber and advance hot blast, start air-introduced machine and an air-introduced machine simultaneously, the liquid material is dried and is solid powder, and be settled down to coolant jacket through king-tower, wind stopping device, air-introduced machine cools off fresh air with solid material material in coolant jacket indirectly in the infall process, the dust material that produces when the sedimentation of solid material enters air loop duct to cyclone separator with the damp-heat air that produces through little gas air inlet and falls into blanking device after heat exchange, fall into the finished product cooling tube again, damp-heat air is discharged by dehumidification tube through air-introduced machine; When opening an air-introduced machine, start the secondary air-introduced machine, the solid material that is fallen into the finished product cooling tube by wind stopping device and blanking device is delivered to cyclone separator No. one time by secondary air-introduced machine air inducing, and fresh air enters the finished product cooling tube through air cleaner the solid material is cooled off.The solid material falls into a blanking device and enters feed bin again, through the baiting valve discharging.The damp-heat air and the dust material that produce in the cooling of solid material enter deduster through a cyclone separator, and damp-heat air is delivered to wet exhauster through the secondary air-introduced machine and discharged, and the dust material falls into a collector again through the baiting valve discharging through deduster.For the ease of rewinding, the madial wall of king-tower, coolant jacket, deduster, feed bin is provided with vibrator, also is provided with compressed air hose on deduster, the feed bin, and it is carried out vibration in timing or air sprays so that blanking.
Claims (5)
1, lauryl alcohol (blowing agent) spray-drying cooling tower, has a king-tower, it is characterized in that: the king-tower top be provided with one with add the central inlet air plenum that warm-air pipe connects, inlet air plenum that at least one communicates with central inlet air plenum by pipeline and at least one with add the secondary air chamber that warm-air pipe connects, the lower end air outlet of central authorities' inlet air plenum in king-tower is provided with homogenating plate one time, the lower end air outlet of an inlet air plenum in king-tower is provided with spray gun, the lower end air outlet of secondary air chamber in king-tower is provided with the secondary homogenating plate, spray gun connects feed voltage-stablizer and high-pressure delivery pump successively by feeder sleeve, tower body middle part arranged outside has with the lower end and has the air loop duct that medial surface that the cyclone separator of blanking device communicates has two little gas air inlets at least, the tower body below is the reverse taper coolant jacket, the upper opening of coolant jacket is equipped with air-introduced machine, the bottom is provided with wind stopping device, wind stopping device, the lower end of blanking device communicates with the finished product cooling tube that an end is provided with air cleaner, the other end of finished product cooling tube and lower end are that a cyclone separator of feed bin communicates, and the top of cyclone separator is by an air-introduced machine, the top of a cyclone separator communicates with wet exhauster by pipeline respectively by the secondary air-introduced machine.
2, lauryl alcohol according to claim 1 (blowing agent) spray-drying cooling tower is characterized in that: also be provided with a deduster between a described cyclone separator and secondary air-introduced machine, the below of deduster is provided with a collector that has baiting valve.
3, lauryl alcohol according to claim 1 and 2 (blowing agent) spray-drying cooling tower is characterized in that: be provided with blanking device one time between a described cyclone separator and feed bin, the feed bin below is provided with baiting valve.
4, lauryl alcohol according to claim 3 (blowing agent) spray-drying cooling tower is characterized in that: described deduster and feed bin top are provided with compressed air hose.
5, lauryl alcohol according to claim 3 (blowing agent) spray-drying cooling tower, it is characterized in that: the madial wall of described king-tower, coolant jacket, dedusting, feed bin is provided with vibrator.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN 01218063 CN2475979Y (en) | 2001-03-27 | 2001-03-27 | Lauryl alcohol (foaming agent) spraying-drying cooling tower |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN 01218063 CN2475979Y (en) | 2001-03-27 | 2001-03-27 | Lauryl alcohol (foaming agent) spraying-drying cooling tower |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN2475979Y true CN2475979Y (en) | 2002-02-06 |
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ID=33636174
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN 01218063 Expired - Fee Related CN2475979Y (en) | 2001-03-27 | 2001-03-27 | Lauryl alcohol (foaming agent) spraying-drying cooling tower |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN2475979Y (en) |
Cited By (6)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN103542706A (en) * | 2012-07-16 | 2014-01-29 | 张洪卫 | Drying system of organoboron production |
| CN103673513A (en) * | 2013-12-31 | 2014-03-26 | 楚雄长青科技有限公司 | Pneumatic drying and ultraviolet sterilizing device of circulating fluidized bed |
| CN103673514A (en) * | 2013-12-31 | 2014-03-26 | 昆明特康科技有限公司 | Pneumatic drying device of circulating fluidized bed |
| CN103712418A (en) * | 2013-12-31 | 2014-04-09 | 昆明特康科技有限公司 | Drying and mixing equipment of circulating fluidized bed |
| CN104251603A (en) * | 2014-09-03 | 2014-12-31 | 嘉善圣莱斯绒业有限公司 | Powder drying device |
| CN105890301A (en) * | 2016-06-07 | 2016-08-24 | 枣庄海川重工机械设备有限公司 | Storage device with drying function |
-
2001
- 2001-03-27 CN CN 01218063 patent/CN2475979Y/en not_active Expired - Fee Related
Cited By (9)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN103542706A (en) * | 2012-07-16 | 2014-01-29 | 张洪卫 | Drying system of organoboron production |
| CN103673513A (en) * | 2013-12-31 | 2014-03-26 | 楚雄长青科技有限公司 | Pneumatic drying and ultraviolet sterilizing device of circulating fluidized bed |
| CN103673514A (en) * | 2013-12-31 | 2014-03-26 | 昆明特康科技有限公司 | Pneumatic drying device of circulating fluidized bed |
| CN103712418A (en) * | 2013-12-31 | 2014-04-09 | 昆明特康科技有限公司 | Drying and mixing equipment of circulating fluidized bed |
| CN103673514B (en) * | 2013-12-31 | 2015-08-26 | 昆明特康科技有限公司 | Recirculating fluidized bed pneumatic conveying dryer |
| CN103673513B (en) * | 2013-12-31 | 2015-08-26 | 楚雄长青科技有限公司 | Recirculating fluidized bed pneumatic conveying drying, ultraviolet sterilization equipment |
| CN103712418B (en) * | 2013-12-31 | 2015-08-26 | 昆明特康科技有限公司 | A kind of recirculating fluidized bed is dry, mixing apparatus |
| CN104251603A (en) * | 2014-09-03 | 2014-12-31 | 嘉善圣莱斯绒业有限公司 | Powder drying device |
| CN105890301A (en) * | 2016-06-07 | 2016-08-24 | 枣庄海川重工机械设备有限公司 | Storage device with drying function |
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Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| C19 | Lapse of patent right due to non-payment of the annual fee | ||
| CF01 | Termination of patent right due to non-payment of annual fee |