CN203990574U - A kind of continuous production horizontal rotary spiral response still - Google Patents
A kind of continuous production horizontal rotary spiral response still Download PDFInfo
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- CN203990574U CN203990574U CN201420420737.4U CN201420420737U CN203990574U CN 203990574 U CN203990574 U CN 203990574U CN 201420420737 U CN201420420737 U CN 201420420737U CN 203990574 U CN203990574 U CN 203990574U
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- reactor housing
- screw rod
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- hand member
- reactor
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Abstract
A continuous production horizontal rotary spiral response still, comprises reactor housing, screw rod, charging aperture, gas discharging opening, liquid outlet opening, decelerator, motor, auxiliary equipment ultrasonic transducer, end cap; Wherein: reactor housing integral body is cylindric, and screw rod is arranged in reactor housing, coaxially arranged, screw rod is with the inwall of reactor housing for contacting moving cooperation, and gas passage is left on top; Charging aperture is positioned at reactor housing left end top, and gas discharging opening is positioned at reactor housing right-hand member top, and liquid outlet opening is positioned at reactor housing right-hand member bottom; Screw rod left end is connected with auxiliary equipment ultrasonic transducer, and the right-hand member of screw rod is connected with motor by decelerator.Advantage of the present utility model: can produce continuously; Control the reaction time of reaction liquid in reactor; By certain time interval newly adding liquid to spaced apart through the liquid having reacted; The solids producing in course of reaction is transported to discharging opening together with liquid.
Description
Technical field
The utility model relates to reactor structure field, particularly a kind of continuous production horizontal rotary spiral response still.
Background technology
Current traditional reactor all adopts tank type, is not easy to realize continuous production, and enabling continuous production can not, by certain time interval newly adding liquid to spaced apart through the liquid having reacted, reduce production efficiency.
Utility model content
The purpose of this utility model is to produce precisely, continuously in order to realize control, and spy provides a kind of continuous production horizontal rotary spiral response still.
The utility model provides a kind of continuous production horizontal rotary spiral response still, it is characterized in that: described continuous production horizontal rotary spiral response still, comprise reactor housing 1, screw rod 2, charging aperture 3, gas discharging opening 4, liquid outlet opening 5, decelerator 6, motor 7, auxiliary equipment ultrasonic transducer 8, end cap 9;
Wherein: reactor housing 1 integral body is cylindric, and screw rod 2 is arranged in reactor housing 1, coaxially arranged, screw rod 2 is with the inwall of reactor housing 1 for contacting moving cooperation, and gas passage is left on top;
Charging aperture 3 is positioned at reactor housing 1 left end top, and gas discharging opening 4 is positioned at reactor housing 1 right-hand member top, and liquid outlet opening 5 is positioned at reactor housing 1 right-hand member bottom;
Screw rod 2 left ends are connected with auxiliary equipment ultrasonic transducer 8, and the right-hand member of screw rod 2 is connected with motor 7 by decelerator 6;
The two ends of reactor housing 1 are all provided with end cap 9.
Described reactor housing 1 inwall, 1/4th places, short transverse top are with the highest liquid level line 10.
Raw material joins after reactor housing 1 reaction liquid under the effect of screw rod 2 is controlled by charging aperture 3 and arrives gas discharging opening by the regular hour, gas is discharged by gas discharging opening 4, the liquid having reacted is discharged by liquid outlet opening 5, the liquid that reaches continuous production the liquid that can react by certain time interval handle and newly add is spaced apart, the length of screw rod 2 and rotating speed can be controlled the reaction time of reaction liquid in reactor, and the diameter dimension of screw rod 2 and helical pitch determine output.
Screw rod 2 is driven and is controlled low speed rotation by motor 7 and decelerator 6, one end of reactor is provided with ultrasonic transducer, can be conducive to the chemical reaction of reactant liquor simultaneously to playing cleaning action in reactor, spiral is when controlling reactant liquor, the solids producing in course of reaction is transported to discharging opening together with liquid, by liquid outlet opening 5, is discharged.
The discontinuous rotation of another working method screw rod 2, raw material utilizes liquid automatic flowing from charging aperture 3 adds, around screw rod 2, flow to discharging opening, the reaction liquid that utilizes screw rod 2 blades that different time is added is spaced apart, can produce continuously and can not make and mix mutually with the liquid through having reacted and the liquid newly adding, 2 of screw rods are done regular rotation.
Advantage of the present utility model:
Continuous production horizontal rotary spiral response still described in the utility model, can produce continuously; Control the reaction time of reaction liquid in reactor; By certain time interval newly adding liquid to spaced apart through the liquid having reacted; The solids producing in course of reaction is transported to discharging opening together with liquid.Can increase external heat or cooling device and select liner and the spiral of different materials, being applied to various liquid needs in quantity-produced consersion unit, such as the consersion unit of various soda acid salts, chlorine dioxide generator etc.
Accompanying drawing explanation
Below in conjunction with drawings and the embodiments, the utility model is described in further detail:
Fig. 1 produces horizontal rotary spiral response still structural representation continuously.
The specific embodiment
Embodiment 1
The present embodiment provides a kind of continuous production horizontal rotary spiral response still, it is characterized in that: described continuous production horizontal rotary spiral response still, comprise reactor housing 1, screw rod 2, charging aperture 3, gas discharging opening 4, liquid outlet opening 5, decelerator 6, motor 7, auxiliary equipment ultrasonic transducer 8, end cap 9;
Wherein: reactor housing 1 integral body is cylindric, and screw rod 2 is arranged in reactor housing 1, coaxially arranged, screw rod 2 is with the inwall of reactor housing 1 for contacting moving cooperation, and gas passage is left on top;
Charging aperture 3 is positioned at reactor housing 1 left end top, and gas discharging opening 4 is positioned at reactor housing 1 right-hand member top, and liquid outlet opening 5 is positioned at reactor housing 1 right-hand member bottom;
Screw rod 2 left ends are connected with auxiliary equipment ultrasonic transducer 8, and the right-hand member of screw rod 2 is connected with motor 7 by decelerator 6;
The two ends of reactor housing 1 are all provided with end cap 9.
Described reactor housing 1 inwall, 1/4th places, short transverse top are with the highest liquid level line 10.
Raw material joins after reactor housing 1 reaction liquid under the effect of screw rod 2 is controlled by charging aperture 3 and arrives gas discharging opening by the regular hour, gas is discharged by gas discharging opening 4, the liquid having reacted is discharged by liquid outlet opening 5, the liquid that reaches continuous production the liquid that can react by certain time interval handle and newly add is spaced apart, the length of screw rod 2 and rotating speed can be controlled the reaction time of reaction liquid in reactor, and the diameter dimension of screw rod 2 and helical pitch determine output.
Screw rod 2 is driven and is controlled low speed rotation by motor 7 and decelerator 6, one end of reactor is provided with ultrasonic transducer, can be conducive to the chemical reaction of reactant liquor simultaneously to playing cleaning action in reactor, spiral is when controlling reactant liquor, the solids producing in course of reaction is transported to discharging opening together with liquid, by liquid outlet opening 5, is discharged.
The discontinuous rotation of another working method screw rod 2, raw material utilizes liquid automatic flowing from charging aperture 3 adds, around screw rod 2, flow to discharging opening, the reaction liquid that utilizes screw rod 2 blades that different time is added is spaced apart, can produce continuously and can not make and mix mutually with the liquid through having reacted and the liquid newly adding, 2 of screw rods are done regular rotation.
Claims (2)
1. produce continuously horizontal rotary spiral response still for one kind, it is characterized in that: described continuous production horizontal rotary spiral response still, comprise reactor housing (1), screw rod (2), charging aperture (3), gas discharging opening (4), liquid outlet opening (5), decelerator (6), motor (7), auxiliary equipment ultrasonic transducer (8), end cap (9);
Wherein: reactor housing (1) integral body is cylindric, and screw rod (2) is arranged in reactor housing (1), coaxially arranged, screw rod (2) is with the inwall of reactor housing (1) for contacting moving cooperation, and gas passage is left on top; Charging aperture (3) is positioned at reactor housing (1) left end top, and gas discharging opening (4) is positioned at reactor housing (1) right-hand member top, and liquid outlet opening (5) is positioned at reactor housing (1) right-hand member bottom;
Screw rod (2) left end is connected with auxiliary equipment ultrasonic transducer (8), and the right-hand member of screw rod (2) is connected with motor (7) by decelerator (6); The two ends of reactor housing (1) are all provided with end cap (9).
2. according to continuous production horizontal rotary spiral response still claimed in claim 1, it is characterized in that: described reactor housing (1) inwall, 1/4th places, short transverse top are with the highest liquid level line (10).
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
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CN201420420737.4U CN203990574U (en) | 2014-07-29 | 2014-07-29 | A kind of continuous production horizontal rotary spiral response still |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN201420420737.4U CN203990574U (en) | 2014-07-29 | 2014-07-29 | A kind of continuous production horizontal rotary spiral response still |
Publications (1)
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CN203990574U true CN203990574U (en) | 2014-12-10 |
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Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
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CN201420420737.4U Expired - Fee Related CN203990574U (en) | 2014-07-29 | 2014-07-29 | A kind of continuous production horizontal rotary spiral response still |
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Cited By (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN108002358A (en) * | 2017-12-08 | 2018-05-08 | 浙江凯圣氟化学有限公司 | The process units and method of a kind of difluorophosphate |
CN109650359A (en) * | 2018-12-29 | 2019-04-19 | 广西越洋科技股份有限公司 | A kind of the industrialization continuous producing apparatus and method of black phosphorus |
-
2014
- 2014-07-29 CN CN201420420737.4U patent/CN203990574U/en not_active Expired - Fee Related
Cited By (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN108002358A (en) * | 2017-12-08 | 2018-05-08 | 浙江凯圣氟化学有限公司 | The process units and method of a kind of difluorophosphate |
CN109650359A (en) * | 2018-12-29 | 2019-04-19 | 广西越洋科技股份有限公司 | A kind of the industrialization continuous producing apparatus and method of black phosphorus |
CN109650359B (en) * | 2018-12-29 | 2020-07-03 | 广西越洋科技股份有限公司 | Industrial continuous production equipment and method for black phosphorus |
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Legal Events
Date | Code | Title | Description |
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C14 | Grant of patent or utility model | ||
GR01 | Patent grant | ||
CF01 | Termination of patent right due to non-payment of annual fee | ||
CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20141210 Termination date: 20170729 |