CN106178562A - For producing the spray dryer of pre-mixing agent - Google Patents

For producing the spray dryer of pre-mixing agent Download PDF

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Publication number
CN106178562A
CN106178562A CN201610539778.9A CN201610539778A CN106178562A CN 106178562 A CN106178562 A CN 106178562A CN 201610539778 A CN201610539778 A CN 201610539778A CN 106178562 A CN106178562 A CN 106178562A
Authority
CN
China
Prior art keywords
cylinder
sound wave
export
port
preheater
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
CN201610539778.9A
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Chinese (zh)
Inventor
廖成斌
卢朝成
蒲鸿涛
唐小洪
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.)
Chengdu Zhongmu Biological Pharmaceutical Co Ltd
Original Assignee
Chengdu Zhongmu Biological Pharmaceutical 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 Chengdu Zhongmu Biological Pharmaceutical Co Ltd filed Critical Chengdu Zhongmu Biological Pharmaceutical Co Ltd
Priority to CN201610539778.9A priority Critical patent/CN106178562A/en
Publication of CN106178562A publication Critical patent/CN106178562A/en
Pending legal-status Critical Current

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Classifications

    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01DSEPARATION
    • B01D1/00Evaporating
    • B01D1/16Evaporating by spraying
    • B01D1/18Evaporating by spraying to obtain dry solids
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01DSEPARATION
    • B01D1/00Evaporating
    • B01D1/14Evaporating with heated gases or vapours or liquids in contact with the liquid
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01DSEPARATION
    • B01D1/00Evaporating
    • B01D1/30Accessories for evaporators ; Constructional details thereof

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  • Chemical & Material Sciences (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Medicinal Preparation (AREA)

Abstract

The invention discloses a kind of spray dryer for producing pre-mixing agent, including support, cylinder and preheater, preheater is provided with at least two airways, airway runs through the top of cylinder and UNICOM's preheater and inner barrel, the port of export of escape pipe is provided with gas distributor, the top of cylinder is provided with feed pipe, the port of export of feed pipe is provided with atomizer, the bottom of cylinder is provided with discharging opening, being provided with two sound wave clear powder devices on the sidewall of cylinder, at least the port of export of a described airway is near the medial wall of cylinder.Use sound wave clear powder device and dry gas purging, the most clear dust effect can be realized, make exsiccator inwall often keep clean state, also do not have powder and adhere to the phenomenon that even high temperature is charred, ensured product quality;By using disturbance and the mechanical agitation effect of the high frequency sound wave of sound wave clear powder device, be conducive to improving dry gas and the heat transfer coefficient of feed liquid, greatly improve drying efficiency.

Description

For producing the spray dryer of pre-mixing agent
Technical field
The present invention relates to a kind of pre-mixing agent manufacturing and processing equipment, be specifically related to a kind of spray drying for producing pre-mixing agent Device.
Background technology
Pre-mixing agent refers to the homogeneous mixture of one or more micro constitutents and diluent or carrier composition.By a kind of or many Kind of medicine and substrate be uniformly mixed for making an addition to feedstuff, for feedstuff medicine interpolation pre-mixing agent.Carrier refers to connect Being subject to and the raised material of carrying powder active ingredient, trace mineral supplement not only can be played diluting effect by it, moreover it is possible to improves and adds The mobility of agent, makes additive be easier to be distributed in feedstuff.Powdery pre-mixing agent for the easy moisture absorption weighs, packs carrying out Need to be dried process before, spray dryer can be used sufficiently to be dried.It is dry that spray dryer is that one has concurrently With the device of pelletize function, its operation principle is that clean air is through heating, the air distribution at entrance spray dryer top Device, hot-air is evenly into hothouse.Feed liquid, through the nebulizer of transport pump to tower body top, sprays into tiny vaporific liquid Pearl, it is with hot-air and flows to contact and is dried rapidly as finished product.Finished product is continuously by bottom exsiccator and follow-up cyclone separator Middle output, waste gas is emptied by air-introduced machine.
Due to the character particularity of powdery pre-mixing agent, existing spray drying technology is susceptible to viscous wall in process of production Phenomenon.Material glues wall and operates not only bad for collecting, and as time went on, the material of heat sensitivity is apt to deteriorate, becomes Defective material.And, adhesion time is long, needs to shut down special cleaning exsiccator inwall, and process is numerous and diverse.
Summary of the invention
The technical problem to be solved is that powdery pre-mixing agent easily occurs viscous wall in spray-drying process, and purpose exists In providing a kind of spray dryer for producing pre-mixing agent, it is achieved remove exsiccator inwall bur continuously, keep high-efficient cleaning Clean state.
The present invention is achieved through the following technical solutions:
A kind of spray dryer for producing pre-mixing agent, including support, cylinder and preheater, described cylinder is fixed on support On, described preheater is provided with at least two airways, and airway runs through the top of cylinder and UNICOM's preheater and inner barrel, leads The port of export of trachea is provided with gas distributor, and the top of cylinder is provided with feed pipe, and the port of export of feed pipe is provided with atomizer, cylinder The bottom of body is provided with discharging opening, and the sidewall of described cylinder is provided with two sound wave clear powder devices, an at least described airway The port of export near the medial wall of cylinder.
In dry run, dry gas is introduced into preheater and carries out the pre-heat treatment so that the gas derived from preheater Having uniform temperature, preheated gas is discharged by gas distributor even in the cylinder of exsiccator by airway.With This simultaneously, feed liquid is imported by feed pipe, and being nebulized by atomizer is contacted with dry gas in drop enters cylinder and reach The purpose being dried.By installing sound wave clear powder device on the sidewall of cylinder morning, exsiccator dry run starts sound wave clear powder device, In barrel space, utilize the concussion effect repeatedly of low-frequency sound wave, put on dust, to stretch the circulation change such as extruding, when When reaching certain cyclic strain number of times, adhere to the bond strength of dust and be destroyed because of repeated strain.Thus can constantly will adhere to Powder on cylinder inboard wall is removed, it is achieved cylinder inboard wall keeps permanent cleaning.Meanwhile, the dry gas entering exsiccator uses Many airways are distributed, and the port of export of an at least described airway is near the medial wall of cylinder, and the program makes along interior The airway high speed air inlet auxiliary sound wave clear powder device dedusting of wall arrangement, improves efficiency of dust collection, ensures that abundant simultaneously It is dried gas and feed liquid and carries out being fully contacted dry.
Described sound wave clear powder device uses high frequency sound wave, and two sound wave clear powder devices are the most staggered also at the sidewall of cylinder It is distributed in the both sides that relative cylinder axle center is symmetrical.
The high frequency sound wave of sound wave clear powder device has higher mechanical agitation relative to low-frequency sound wave to dry gas and feed liquid and makees With, and by the most staggered for two sound wave clear powder devices and be distributed in symmetrical both sides, relative cylinder axle center can to increase sound wave clear Powder device is to dry gas and the perturbation action of feed liquid, thus is conducive to increasing both convective heat-transfer coefficients, can improve dry greatly Dry efficiency.
The port of export of described feed pipe is provided with distribution plate, and described distribution plate is evenly distributed with at least three atomizer.
By installing distribution plate at feed inlet end, atomizer is evenly spaced on distributing disc, and beneficially feed liquid is with vaporific Drop is uniformly sprayed in cylinder, contributes to the contact area increasing drop with dry gas, improves heat transfer efficiency.
The present invention compared with prior art, has such advantages as and beneficial effect:
1, a kind of spray dryer for producing pre-mixing agent of the present invention, uses sound wave clear powder device and dry gas purging, can be real Now continuous clear dust effect, makes exsiccator inwall often keep clean state, does not also have powder and adheres to even high temperature and be charred Phenomenon, ensured product quality;
2, a kind of spray dryer for producing pre-mixing agent of the present invention, by using the disturbance of the high frequency sound wave of sound wave clear powder device With mechanical agitation effect, be conducive to improving dry gas and the heat transfer coefficient of feed liquid, greatly improve drying efficiency.
Accompanying drawing explanation
Accompanying drawing described herein is used for providing being further appreciated by the embodiment of the present invention, constitutes of the application Point, it is not intended that the restriction to the embodiment of the present invention.In the accompanying drawings:
Fig. 1 is present configuration schematic diagram;
Fig. 2 is distributing disc structural representation of the present invention;
The parts title of labelling and correspondence in accompanying drawing: 1-feed pipe, 2-preheater, 3-airway, 4-cylinder, 5-gas is distributed Device, 6-sound wave clear powder device, 7-support, 8-distribution plate, 9-atomizer, 10-discharging opening.
Detailed description of the invention
For making the object, technical solutions and advantages of the present invention clearer, below in conjunction with embodiment and accompanying drawing, to this Invention is described in further detail, and the exemplary embodiment of the present invention and explanation thereof are only used for explaining the present invention, do not make For limitation of the invention.
Embodiment
As it is shown in figure 1, a kind of spray dryer for producing pre-mixing agent of the present invention, including support 7, cylinder 4 and preheating Device 2.Cylinder 4 is fixed on support 7, and preheater 2 is provided with two airways 3, and the port of export of two airways 3 is near cylinder The medial wall of 4.Airway 3 runs through the top of cylinder 4 and UNICOM's preheater 2 and cylinder 4 is internal, and the port of export of escape pipe 3 is arranged There is gas distributor 5.The top of cylinder 4 is provided with feed pipe 1, and the port of export of feed pipe 1 is provided with distribution plate 8, on distribution plate 8 all Even it is placed with nine atomizers 9.Being provided with two sound wave clear powder devices 6 on the sidewall of cylinder 4, sound wave clear powder device 6 uses high frequency Sound wave, and two sound wave clear powder devices 6 the most staggered at the sidewall of cylinder 4 and be distributed in that relative cylinder 4 axle center is symmetrical two Side.The bottom of cylinder 4 is provided with discharging opening 10.
Above-described detailed description of the invention, has been carried out the purpose of the present invention, technical scheme and beneficial effect further Describe in detail, be it should be understood that the detailed description of the invention that the foregoing is only the present invention, be not intended to limit the present invention Protection domain, all within the spirit and principles in the present invention, any modification, equivalent substitution and improvement etc. done, all should comprise Within protection scope of the present invention.

Claims (3)

1. for producing a spray dryer for pre-mixing agent, including support (7), cylinder (4) and preheater (2), described cylinder (4) being fixed on support (7), described preheater (2) is provided with at least two airways (3), and airway (3) runs through cylinder (4) top Portion and connection preheater (2) and cylinder (4) inside, the port of export of airway (3) is provided with gas distributor (5), the top of cylinder (4) Portion is provided with feed pipe (1), and the port of export of feed pipe (1) is provided with atomizer (9), and the bottom of cylinder (4) is provided with discharging opening (10), It is characterized in that, the sidewall of described cylinder (4) is provided with two sound waves clear powder device (6), at least a described airway (3) The port of export near the medial wall of cylinder (4).
A kind of spray dryer for producing pre-mixing agent the most according to claim 1, it is characterised in that described sound wave is clear Powder device (6) uses high frequency sound wave, and two sound waves clear powder device (6) are the most staggered at the sidewall of cylinder (4) and are distributed in phase The both sides symmetrical to cylinder (4) axle center.
A kind of spray dryer for producing pre-mixing agent the most according to claim 1, it is characterised in that described feed pipe (1) the port of export is provided with distribution plate (8), and distribution plate (8) is evenly distributed with at least three atomizer (9).
CN201610539778.9A 2016-07-11 2016-07-11 For producing the spray dryer of pre-mixing agent Pending CN106178562A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN201610539778.9A CN106178562A (en) 2016-07-11 2016-07-11 For producing the spray dryer of pre-mixing agent

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN201610539778.9A CN106178562A (en) 2016-07-11 2016-07-11 For producing the spray dryer of pre-mixing agent

Publications (1)

Publication Number Publication Date
CN106178562A true CN106178562A (en) 2016-12-07

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Application Number Title Priority Date Filing Date
CN201610539778.9A Pending CN106178562A (en) 2016-07-11 2016-07-11 For producing the spray dryer of pre-mixing agent

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Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN112245946A (en) * 2020-10-09 2021-01-22 宁波鼎科新材料科技有限公司 Processing technology of plant extract concentrated solution

Citations (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN204319789U (en) * 2014-12-17 2015-05-13 江西南昌制药有限公司 A kind of Highspeedcentrifugingandsprayingdrier
CN105013201A (en) * 2015-08-11 2015-11-04 山东泰诺药业有限公司 Centrifugal spray dryer
CN205832655U (en) * 2016-07-11 2016-12-28 成都中牧生物药业有限公司 Pre-mixing agent spray dryer

Patent Citations (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN204319789U (en) * 2014-12-17 2015-05-13 江西南昌制药有限公司 A kind of Highspeedcentrifugingandsprayingdrier
CN105013201A (en) * 2015-08-11 2015-11-04 山东泰诺药业有限公司 Centrifugal spray dryer
CN205832655U (en) * 2016-07-11 2016-12-28 成都中牧生物药业有限公司 Pre-mixing agent spray dryer

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN112245946A (en) * 2020-10-09 2021-01-22 宁波鼎科新材料科技有限公司 Processing technology of plant extract concentrated solution
CN112245946B (en) * 2020-10-09 2021-12-21 河源市吉龙翔生物科技有限公司 Processing technology of plant extract concentrated solution

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Application publication date: 20161207

RJ01 Rejection of invention patent application after publication