CN105135853A - Stearic acid salt drying control device - Google Patents

Stearic acid salt drying control device Download PDF

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Publication number
CN105135853A
CN105135853A CN201510560173.3A CN201510560173A CN105135853A CN 105135853 A CN105135853 A CN 105135853A CN 201510560173 A CN201510560173 A CN 201510560173A CN 105135853 A CN105135853 A CN 105135853A
Authority
CN
China
Prior art keywords
drying
control
stearate
dry wind
drying box
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Pending
Application number
CN201510560173.3A
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Chinese (zh)
Inventor
吴亮
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.)
Fa Base Chemicals (zhangjiagang) Co Ltd
Original Assignee
Fa Base Chemicals (zhangjiagang) Co Ltd
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by Fa Base Chemicals (zhangjiagang) Co Ltd filed Critical Fa Base Chemicals (zhangjiagang) Co Ltd
Priority to CN201510560173.3A priority Critical patent/CN105135853A/en
Publication of CN105135853A publication Critical patent/CN105135853A/en
Pending legal-status Critical Current

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Abstract

The invention discloses a stearic acid salt drying control device. The control device comprises a drying box, a material entering pipe, a material outlet, a drying air inlet and a drying air outlet. A cloth bag type filter is arranged above the drying box. A material conveying auger is arranged at the inner bottom of the drying box. An auger engine is arranged at the bottom of the outer right side of the drying box. A filter blowing air inlet is formed in the upper portion of the left side of the cloth bag type filter. The drying air outlet is formed in the upper portion of the right side of the cloth bag type filter. The material entering pipe is located in the middle of the outer left side of the drying box and connected with the drying air inlet. A steam jacket is arranged on the outer side of the material entering pipe. The material outlet is located in the bottom of the outer side of the drying box. According to the stearic acid salt drying control device, the principle that water in products is taken away by means of the unsaturation degree of water in air and evaporation phase combination caused after water is released through high pressure is used, the steam jacket is arranged outside the material entering pipe, the temperature of materials and drying air is raised, the higher the temperature of drying air is, the higher the unsaturation degree of water is, and therefore vaporized water in stearic acid salt can be taken away.

Description

A kind of stearate apparatus for control of drying
Technical field
The invention belongs to chemical mechanical equipment field, be specifically related to a kind of stearate apparatus for control of drying.
Background technology
In stearates production process, the control of moisture is the technical barrier in conventional production methods always, and the moisture sloughed in stearates also becomes the emphasis of production technology.Because the characteristic of stearates is the moisture easily absorbed in air; so conventional centrifuge usually can be used to make the moisture in stearate series products deviate from; but conventional method not only inefficiency in this, and be subject to the impact of production environment temperature, the restriction be subject in process of production is large.
Summary of the invention
For solving the problem, the invention discloses a kind of stearate apparatus for control of drying, to be used for solving the problem.
For achieving the above object, technical scheme of the present invention is as follows:
A kind of stearate apparatus for control of drying, comprise drying box, material inlet pipe, material outlet, dry wind entrance, dry wind exports, above described drying box, bag filter is set, drying box inner bottom part arranges material conveyor, auger engine is set bottom drying box external right side, be connected with materials inside conveying auger, on the left of described bag filter, top arranges filter and purges air inlet, top, right side arranges dry wind outlet, described material inlet pipe is positioned at the outer left side central portion of drying box, material inlet pipe arranged outside steam jacket, material inlet pipe connects dry wind entrance, described material outlet is positioned at drying box exterior bottom.
As a modification of the present invention, described bag filter inside arranges metallic support.
As a modification of the present invention, in described steam jacket, vapor (steam) temperature is greater than 150 DEG C.
As a modification of the present invention, described dry wind entrance connects inflator pump.
As a modification of the present invention, described dry wind outlet connects aspiration pump.
As a modification of the present invention, described dry wind outlet temperature is at 45 DEG C ~ 48 DEG C.
As a modification of the present invention, described dry wind moisture is lower than 20%.
As a modification of the present invention, the angle of described dry wind entrance and material inlet pipe is less than 90 °.
The invention has the beneficial effects as follows:
A kind of stearate apparatus for control of drying of the present invention, vaporize after utilizing the degree of unsaturation of water in air to be discharged by high pressure with water to combine, by the principle that the water in product is taken away by air, outside material inlet pipe, steam jacket is set, material and dry air are heated, drying air temperature is higher, and the degree of unsaturation of water is also higher, so can take away the moisture content of vaporizing in stearate.
Accompanying drawing explanation
Fig. 1 is structural representation of the present invention.
Reference numerals list:
1. drying box, 2. material inlet pipe, 3. dry wind entrance, 4. steam jacket, 5. dry wind outlet, 6. bag filter, 7. filter purges air inlet, 8. auger engine, 9. material conveyor, 10. material outlet.
Detailed description of the invention
Below in conjunction with the drawings and specific embodiments, illustrate the present invention further, following detailed description of the invention should be understood and be only not used in for illustration of the present invention and limit the scope of the invention.It should be noted that, the word "front", "rear" of use is described below, "left", "right", "up" and "down" refer to direction in accompanying drawing, word " interior " and " outward " refer to the direction towards or away from particular elements geometric center respectively.
As shown in the figure, a kind of stearate apparatus for control of drying, comprise drying box 1, material inlet pipe 2, material outlet 10, dry wind entrance 3, dry wind outlet 5, above described drying box 1, bag filter 6 is set, bag filter 6 inside arranges metallic support, can guarantee that dry wind can not take away stearate, bag filter 6 can not be out of shape because of air flowing to use metallic support also can ensure, on the left of bag filter 6, top arranges filter and purges air inlet 7, the stearate sticking to bag filter 6 surface can be blown off, bag filter 6 can not be blocked.
As shown in the figure, drying box 1 inner bottom part arranges material conveyor 9, arranges auger engine 8 bottom drying box 1 external right side, be connected with materials inside conveying auger 9, auger by constantly rotating, can make stearate fully contact with air, and ensureing that stearate can not lump.
As shown in the figure, arrange dry wind outlet 5 above right side, dry wind outlet 5 connects aspiration pump, and dry wind entrance 3 connects inflator pump, fully can ensure the flowing of dry air.
As shown in the figure, described material inlet pipe 2 is positioned at the outer left side central portion of drying box 1, material inlet pipe 2 arranged outside steam jacket 4, and material inlet pipe 2 connects dry wind entrance 3, and described material outlet 10 is positioned at drying box 1 exterior bottom.
As shown in the figure, in described steam jacket 4, vapor (steam) temperature is greater than 150 DEG C, can ensure that the temperature of stearate and dry air raises.
As shown in the figure, described dry wind exports 5 temperature at 45 DEG C ~ 48 DEG C, can not lower the degree of unsaturation of water because drying air temperature reduces.
As shown in the figure, described dry wind moisture, lower than 20%, guarantees to take away enough moisture.
As shown in the figure, described dry wind entrance 3 is less than 90 ° with the angle of material inlet pipe 2, can enter drying box 1 with the same direction of stearate.
Technological means disclosed in the present invention program is not limited only to the technological means disclosed in above-mentioned embodiment, also comprises the technical scheme be made up of above technical characteristic.

Claims (8)

1. a stearate apparatus for control of drying, it is characterized in that: comprise drying box, material inlet pipe, material outlet, dry wind entrance, dry wind exports, above described drying box, bag filter is set, drying box inner bottom part arranges material conveyor, auger engine is set bottom drying box external right side, be connected with materials inside conveying auger, on the left of described bag filter, top arranges filter and purges air inlet, top, right side arranges dry wind outlet, described material inlet pipe is positioned at the outer left side central portion of drying box, material inlet pipe arranged outside steam jacket, material inlet pipe connects dry wind entrance, described material outlet is positioned at drying box exterior bottom.
2. a kind of stearate apparatus for control of drying according to claim 1, is characterized in that: described bag filter inside arranges metallic support.
3. a kind of stearate apparatus for control of drying according to claim 1, is characterized in that: in described steam jacket, vapor (steam) temperature is greater than 150 DEG C.
4. a kind of stearate apparatus for control of drying according to claim 1, is characterized in that: described dry wind entrance connects inflator pump.
5. a kind of stearate apparatus for control of drying according to claim 1, is characterized in that: described dry wind outlet connects aspiration pump.
6. a kind of stearate apparatus for control of drying according to claim 1, is characterized in that: described dry wind outlet temperature is at 45 DEG C ~ 48 DEG C.
7. a kind of stearate apparatus for control of drying according to claim 1, is characterized in that: described dry wind moisture is lower than 20%.
8. a kind of stearate apparatus for control of drying according to claim 1, is characterized in that: the angle of described dry wind entrance and material inlet pipe is less than 90 °.
CN201510560173.3A 2015-09-07 2015-09-07 Stearic acid salt drying control device Pending CN105135853A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN201510560173.3A CN105135853A (en) 2015-09-07 2015-09-07 Stearic acid salt drying control device

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN201510560173.3A CN105135853A (en) 2015-09-07 2015-09-07 Stearic acid salt drying control device

Publications (1)

Publication Number Publication Date
CN105135853A true CN105135853A (en) 2015-12-09

Family

ID=54721299

Family Applications (1)

Application Number Title Priority Date Filing Date
CN201510560173.3A Pending CN105135853A (en) 2015-09-07 2015-09-07 Stearic acid salt drying control device

Country Status (1)

Country Link
CN (1) CN105135853A (en)

Citations (9)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US4809442A (en) * 1985-12-27 1989-03-07 Tdk Corporation Spray drying process and apparatus therefor
US20100170854A1 (en) * 2009-01-06 2010-07-08 Severn Trent De Nora, Llc Sludge Dewatering and Drying
CN103344093A (en) * 2013-06-09 2013-10-09 山东奥诺能源科技有限公司 Vertical type continuous fluidized bed pelleting drying device and method
CN203518421U (en) * 2013-09-23 2014-04-02 浙江海昇化学有限公司 Horizontal-type fluidized drying machine
CN203518417U (en) * 2013-08-30 2014-04-02 南京华星制药设备有限公司 Improved fluidized drying machine
CN104034128A (en) * 2014-06-10 2014-09-10 张家港市杨舍丝印工艺厂 Intermittent closed-pipeline fluidized drying device and method
CN204301413U (en) * 2014-11-30 2015-04-29 江西麒麟化工有限公司 Boiling drier
CN204388468U (en) * 2014-12-31 2015-06-10 淮北新兴实业有限责任公司 A kind of fluidized drying device for ALANINE
CN205066372U (en) * 2015-09-07 2016-03-02 发基化学品(张家港)有限公司 Stearate drying control device

Patent Citations (9)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US4809442A (en) * 1985-12-27 1989-03-07 Tdk Corporation Spray drying process and apparatus therefor
US20100170854A1 (en) * 2009-01-06 2010-07-08 Severn Trent De Nora, Llc Sludge Dewatering and Drying
CN103344093A (en) * 2013-06-09 2013-10-09 山东奥诺能源科技有限公司 Vertical type continuous fluidized bed pelleting drying device and method
CN203518417U (en) * 2013-08-30 2014-04-02 南京华星制药设备有限公司 Improved fluidized drying machine
CN203518421U (en) * 2013-09-23 2014-04-02 浙江海昇化学有限公司 Horizontal-type fluidized drying machine
CN104034128A (en) * 2014-06-10 2014-09-10 张家港市杨舍丝印工艺厂 Intermittent closed-pipeline fluidized drying device and method
CN204301413U (en) * 2014-11-30 2015-04-29 江西麒麟化工有限公司 Boiling drier
CN204388468U (en) * 2014-12-31 2015-06-10 淮北新兴实业有限责任公司 A kind of fluidized drying device for ALANINE
CN205066372U (en) * 2015-09-07 2016-03-02 发基化学品(张家港)有限公司 Stearate drying control device

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Application publication date: 20151209