CN102059073A - Tumbler sulfur granulator with two discharging ends - Google Patents
Tumbler sulfur granulator with two discharging ends Download PDFInfo
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- CN102059073A CN102059073A CN2010105438279A CN201010543827A CN102059073A CN 102059073 A CN102059073 A CN 102059073A CN 2010105438279 A CN2010105438279 A CN 2010105438279A CN 201010543827 A CN201010543827 A CN 201010543827A CN 102059073 A CN102059073 A CN 102059073A
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- rotating cylinder
- sulphur
- cooling water
- sulfur
- comminutor
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Abstract
The invention relates to a tumbler sulfur granulator with two discharging ends, which is characterized by comprising a tumbler, a sulfur jacketed pipe, a sulfur nozzle, a cooling water pipe, a cooling water nozzle, large supporting roller rings, a small supporting roller, a large gear ring, a pinion, a motor reducer, seal covers and a base, wherein two large supporting roller rings are installed on the tumbler; the large gear ring, the pinion cooperated with the large gear ring and the gear reducer driving the pinion are installed between the large supporting roller rings; the seal covers are installed on two end surfaces of the tumbler; the jacketed pipe and the cooling water pipe which are fixed on the seal covers at two ends do not rotate with the tumbler, and solidified sulfur granules overflow from circular slices on the two ends of the tumbler; the sulfur nozzle is installed on the sulfur jacketed pipe; the cooling water nozzle is installed on the cooling water pipe; and the two large supporting roller rings and the small supporting roller on the base form a triangle support. The invention has the advantages that 6-30 tons of granule sulfur products can be obtained per hour by using the granulator, and the diameter of the produced spherical sulfur granules is 1.0-6 millimeters; the maximum production capacity is high, the occupied area is small, the investment is saved, and the production cost is low.
Description
Technical field:
What the present invention relates to is a kind of rotating cylinder sulphur comminutor that liquid-state sulfur is solidify to form the two ends discharging of spheric granules.Belong to the Chemical Manufacture field of mechanical technique.
Background technology:
Sulphur is a kind of byproduct that produces in the oil and natural gas sweetening process of producing.At present, the mode of processing sulphur has: 1. Molten sulphur is directly injected the sulphur pond and solidify to form irregular bulk, but produce dust polluting environment in transportation.2. Molten sulphur is directly delivered in the factory of downstream with thermal insulating tank car.But the ability that is subjected to transportation range and downstream factory now limits.3. adopt the steel band comminutor, see patent CN200420108449.1, CN99224713.6, CN200420030205.6, CN98238065.8.This device is owing to be subjected to the restriction of width of steel band and granulation is only carried out two factors of two dimensional surface cloth in steel strip surface and restricted.Cause on steel band sulphur production capacity maximum to have only 6 tons/hour.This machinery is that sulphur granulation production occasion more than 6 tons/hour is inapplicable because floor space is big in output.4. adopt rotating cylinder sulphur comminutor, see Chinese patent 200820238258.5 rotating cylinder sulphur comminutors.This structure is single-ended discharging, causes drusen long in rotating cylinder the inside time of staying, and the particle friction easily produces dust, and particle is bigger.Improve the output rotating cylinder that can only extend, cause equipment volume huge.
Summary of the invention:
What the present invention proposed is a kind of rotating cylinder sulphur comminutor that liquid-state sulfur is solidify to form the two ends discharging of spheric granules; its purpose is intended to overcome the above-mentioned defective of existing in prior technology; have and can produce 6 ~ 30 tons of/hour spherical sulfur granules, the particle diameter of controlling solid sulfur simultaneously is between 1 ~ 6 millimeter.
Technical solution of the present invention: it is characterized in that comprising rotating cylinder, the sulphur jacket pipe, the sulphur shower nozzle, cooling water pipe, water-cooling-sprayer, the big supporting wheel circle, little support roller, bull gear, pinion, motor reducer, seal closure and base, 2 big supporting wheel circles wherein are installed on the rotating cylinder, 1 bull gear and the pinion that cooperates with it and the motor reducer of driving pinion are installed between 2 big supporting wheel circles, the rotating cylinder both ends of the surface are installed seal closure, jacket pipe and cooling water pipe are fixed on the seal closure at two ends, do not rotate with rotating cylinder, drusen after the curing overflows from the annular weir plate at rotating cylinder two ends, the sulphur shower nozzle is installed on the sulphur jacket pipe, adorn water-cooling-sprayer on the cooling water pipe, 2 big supporting wheel circles and be installed in individual little support roller support triangular in shape on the base.
Advantage of the present invention: this machinery can guarantee to obtain the 6-30 ton/hour the particle sulfur product, the sulphur of production is 1. ~ 6 millimeters spheric granules.The present invention has that big production capacity, floor space are little, reduced investment, characteristics such as reduce production costs.
Description of drawings
Accompanying drawing 1 is the rotating cylinder sulphur comminutor of two ends discharging
Accompanying drawing 2 is A-A cut-away views among Fig. 1.
Among the figure 1 is rotating cylinder, the 2nd, sulphur jacket pipe, the 3rd, sulphur shower nozzle, the 4th, cooling water pipe, the 5th, water-cooling-sprayer, the 6th, big supporting wheel circle, the 7th, little support roller, the 8th, bull gear, the 9th, pinion, the 10th, motor reducer, the 11st, seal closure, the 12nd, base, the 1.1st, flight, the 1.2nd, circular discharging weir plate.
The specific embodiment
The contrast accompanying drawing, its structure comprises rotating cylinder 1, sulphur jacket pipe 2, sulphur shower nozzle 3, cooling water pipe 4, water-cooling-sprayer 5, big supporting wheel circle 6, little support roller 7, bull gear 8, pinion 9, motor reducer 10, seal closure 11 and base 12,2 big supporting wheel circles 6 wherein are installed on the rotating cylinder 1,1 bull gear 8 and the pinion 9 that cooperates with it and the motor reducer 10 of driving pinion are installed between 2 big supporting wheel circles 6, rotating cylinder 1 both ends of the surface are installed seal closure 11, jacket pipe 2 and cooling water pipe 4 are fixed on the seal closure 11 at two ends, do not rotate with rotating cylinder, drusen after the curing overflows from the annular weir plate 1.2 at rotating cylinder 1 two ends, sulphur shower nozzle 3 is installed on the sulphur jacket pipe 2,5,2 big supporting wheel circles of dress water-cooling-sprayer 6 and 4 little support roller 7 supports triangular in shape that are installed on the base 12 on the cooling water pipe 4.
Molten sulphur is transformed into 1 ~ 6 millimeter spherical solid drusen.
It is 8 ~ 50 flights 1.1 that rotating cylinder 1 inwall is evenly installed quantity; Both ends of the surface are respectively installed 1 highly identical circular discharging weir plate 1.2.
Near rotating cylinder two ends outer wall 1 big supporting wheel circle 6 is being installed respectively, per 2 little support rollers 7 support 1 big supporting wheel circle 6;
Little roller bracket, pinion support, gear wheel support and motor reducer 10 are installed on base 12.
The rotation of rotating cylinder and horizontal plane angle are zero degree.
When rotating cylinder 1 by after the driven by motor rotation, the Molten sulphur that has pressure is transported to the porch of sulphur jacket pipe 2 and by the sulphur shower nozzle 3 on the jacket pipe, molten sulfur is sprayed into atomised form carry out granulation in the rotating cylinder 1.For making the Molten sulphur cooling curing form solid particle; Have simultaneously that the cooling water of pressure is transported to the porch of cooling water pipe 4 after pressurized and by the water-cooling-sprayer on the cooling water pipe 5, spray in the rotating cylinder 1 with the form of atomizing.Drusen after the curing overflows from the annular weir plate at rotating cylinder 1 two ends.Inner surface is installed 8 ~ 50 flights 1.1 in rotating cylinder; Evenly distribute along rotating cylinder inner surface circumferencial direction.A height respectively be installed be 10 ~ 500 millimeters high annular discharging weir plate at the revolving drum granulator two ends.Rotating cylinder is by 2 big supporting wheels 6 that are installed in its outer surface and 4 little support roller 7 supports triangular in shape that are installed on the base 12; And drive bull gear 8 rotations that are installed on the rotating cylinder by pinion 9 by motor reducer 10; Thereby make whole rotating cylinder rotation.The chuck sulphur pipe 2 that 2 ~ 30 sulphur shower nozzles 3 are installed gos deep in the rotating cylinder vertically; While sulphur tube center distance rotating cylinder center line is greater than more than 200 millimeters, and the plane parallel of rotating cylinder center line and the formation of sulphur tube hub line is in horizontal plane.The sulphur pipe is the chuck insulating tube, and the chuck layer adopts 0.3 ~ 0.6Mpa steam or 150 ° ~ 160 ° conduction oils companion heat, prevents that Molten sulphur from solidifying in pipe.The water pipe that has 2 ~ 30 water-cooling-sprayers stretches in the rotating cylinder vertically; Parallel with the sulphur jacket pipe and be positioned at its below.The sulphur shower nozzle is vertical tube rotaring axis with the water-cooling-sprayer injection direction.The cooling water pipe inlet links to each other by pipeline with cooling water source.
Production process is implemented as follows: after above-mentioned machinery is installed by summary of the invention.Add a part drusen or the powder of cooling curing in rotating cylinder sulphur comminutor, the annular discharging weir plate that adds controlling level and rotating cylinder two ends maintains an equal level and gets final product.This moment, but starter motor drove the rotating cylinder rotation.The powder of observing in the cylinder is got up to form multilayer material curtain in tube by flight.Starting cooling water pump is sprayed on the cooling water pressurization on the material curtain of formation through rotating cylinder sulphur comminutor water-cooling-sprayer formation water smoke shape.Subsequently Molten sulphur is pressed and delivered to liquid sulfur pump in the chuck sulphur pipe that has the sulphur shower nozzle in the revolving drum granulator, by the sulphur shower nozzle Molten sulphur is formed fine drop and be sprayed on the powder curtain of being taken up by flight with bonding mixing of powder and form particle and under the gravity effect, fall.In the process that falls, be installed in the atomizing cool water shower cooling below the sulphur pipe, solidify to form spheric granules.Finally fall into the cylinder bottom and taken up once more, also be atomized cooling water temperature again by the Molten sulphur parcel again by flight.Go round and begin again like this, particle is grown up gradually and is spherical shape.Along with the increase of inventory, material level surpasses cylinder two ends weir plate gradually and is discharged from cylinder from rotating cylinder sulphur comminutor two ends.Because rotating cylinder is two ends dischargings simultaneously; therefore drusen time of staying in rotating cylinder is 1/2nd of single-ended discharging; the revolving drum granulator of therefore same length; the revolving drum granulator granular size of both-end discharging is 1/2nd of single-ended discharging, and the particle dust that collision friction produces in rotating cylinder reduces 50 percent.By such scheme, the spherical sulfur granules that obtains has reached and has both formed the high yield drusen product smaller particles of getting back in 1 ~ 6 millimeter scope, has reduced dust pollution simultaneously.
Claims (7)
1. the rotating cylinder sulphur comminutor of a two ends discharging; it is characterized in that comprising rotating cylinder; the sulphur jacket pipe; the sulphur shower nozzle; cooling water pipe; water-cooling-sprayer; the big supporting wheel circle; little support roller; bull gear; pinion; motor reducer; seal closure and base; 2 big supporting wheel circles wherein are installed on the rotating cylinder; 1 bull gear and the pinion that cooperates with it and the motor reducer of driving pinion are installed between 2 big supporting wheel circles; the rotating cylinder both ends of the surface are installed seal closure; jacket pipe and cooling water pipe are fixed on the seal closure at two ends; do not rotate with rotating cylinder; drusen after the curing overflows from the annular weir plate at rotating cylinder two ends; the sulphur shower nozzle is installed on the sulphur jacket pipe; adorn water-cooling-sprayer on the cooling water pipe, 2 big supporting wheel circles and be installed in individual little support roller support triangular in shape on the base.
2. want the rotating cylinder sulphur comminutor of 1 described a kind of two ends discharging according to right, it is characterized in that Molten sulphur is transformed into 1 ~ 6 millimeter spherical solid drusen.
3. want the rotating cylinder sulphur comminutor of 1 described a kind of two ends discharging according to right, it is characterized in that it is 8 ~ 50 flights that the rotating cylinder inwall is evenly installed quantity; Both ends of the surface are respectively installed 1 highly identical circular discharging weir plate.
4. want the rotating cylinder sulphur comminutor of 1 described a kind of two ends discharging according to right, it is characterized in that near rotating cylinder two ends outer wall big supporting wheel circle being installed respectively, per 2 little support rollers support 1 big supporting wheel circle.
5. want the rotating cylinder sulphur comminutor of 1 described a kind of two ends discharging according to right, it is characterized in that on base, installing little roller bracket, pinion support, gear wheel support and motor reducer.
6. want the rotating cylinder sulphur comminutor of 1 described a kind of two ends discharging according to right, it is characterized in that the rotation of rotating cylinder and horizontal plane angle are zero degree.
7. want the rotating cylinder sulphur comminutor of 1 described a kind of two ends discharging according to right, it is characterized in that sulphur shower nozzle and water-cooling-sprayer injection direction are vertical tube rotaring axis, the cooling water pipe inlet links to each other by pipeline with cooling water source.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN 201010543827 CN102059073B (en) | 2010-11-15 | 2010-11-15 | Tumbler sulfur granulator with two discharging ends |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN 201010543827 CN102059073B (en) | 2010-11-15 | 2010-11-15 | Tumbler sulfur granulator with two discharging ends |
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| Publication Number | Publication Date |
|---|---|
| CN102059073A true CN102059073A (en) | 2011-05-18 |
| CN102059073B CN102059073B (en) | 2013-01-30 |
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| Application Number | Title | Priority Date | Filing Date |
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| CN 201010543827 Active CN102059073B (en) | 2010-11-15 | 2010-11-15 | Tumbler sulfur granulator with two discharging ends |
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Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN102716690A (en) * | 2012-06-20 | 2012-10-10 | 江苏洪流化工机械有限公司 | Improved horizontal vessel rotating device |
| CN110639427A (en) * | 2018-12-10 | 2020-01-03 | 金昌正旭工贸有限责任公司 | Sulfur molten liquid spraying water-cooling medium granulation process |
| CN111804239A (en) * | 2020-06-11 | 2020-10-23 | 盐城市锦东液压机械有限公司 | Sealed rotary joint of reactor |
Citations (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN1597123A (en) * | 2004-09-17 | 2005-03-23 | 郝志刚 | Milling mechanism of horizontal grinder |
| CN201100826Y (en) * | 2007-08-27 | 2008-08-13 | 山东天力干燥设备有限公司 | Turning cylinder drier with feed guide device |
| CN201161183Y (en) * | 2007-11-29 | 2008-12-10 | 常州先锋干燥设备有限公司 | Granulator |
| CN201357065Y (en) * | 2008-12-26 | 2009-12-09 | 南京三普造粒装备有限公司 | Rotary drum sulfur granulator |
-
2010
- 2010-11-15 CN CN 201010543827 patent/CN102059073B/en active Active
Patent Citations (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN1597123A (en) * | 2004-09-17 | 2005-03-23 | 郝志刚 | Milling mechanism of horizontal grinder |
| CN201100826Y (en) * | 2007-08-27 | 2008-08-13 | 山东天力干燥设备有限公司 | Turning cylinder drier with feed guide device |
| CN201161183Y (en) * | 2007-11-29 | 2008-12-10 | 常州先锋干燥设备有限公司 | Granulator |
| CN201357065Y (en) * | 2008-12-26 | 2009-12-09 | 南京三普造粒装备有限公司 | Rotary drum sulfur granulator |
Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN102716690A (en) * | 2012-06-20 | 2012-10-10 | 江苏洪流化工机械有限公司 | Improved horizontal vessel rotating device |
| CN110639427A (en) * | 2018-12-10 | 2020-01-03 | 金昌正旭工贸有限责任公司 | Sulfur molten liquid spraying water-cooling medium granulation process |
| CN111804239A (en) * | 2020-06-11 | 2020-10-23 | 盐城市锦东液压机械有限公司 | Sealed rotary joint of reactor |
Also Published As
| Publication number | Publication date |
|---|---|
| CN102059073B (en) | 2013-01-30 |
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