CN205850823U - Metallic catalyst reduction apparatus - Google Patents

Metallic catalyst reduction apparatus Download PDF

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Publication number
CN205850823U
CN205850823U CN201620814041.9U CN201620814041U CN205850823U CN 205850823 U CN205850823 U CN 205850823U CN 201620814041 U CN201620814041 U CN 201620814041U CN 205850823 U CN205850823 U CN 205850823U
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CN
China
Prior art keywords
reduction
reduction furnace
furnace
accesses
metallic catalyst
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.)
Expired - Fee Related
Application number
CN201620814041.9U
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Chinese (zh)
Inventor
赵金胜
路鹏
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.)
BAIYIN YANGMING YINGUANG CHEMICAL CO LTD
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BAIYIN YANGMING YINGUANG CHEMICAL CO LTD
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Priority to CN201620814041.9U priority Critical patent/CN205850823U/en
Application granted granted Critical
Publication of CN205850823U publication Critical patent/CN205850823U/en
Expired - Fee Related legal-status Critical Current
Anticipated expiration legal-status Critical

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Abstract

This utility model relates to a kind of metallic catalyst reduction apparatus, it is characterised in that: reduction furnace (1) furnace body outer wall is provided with heat-insulation layer (4), and heat-insulation layer (4) is externally provided with thermal insulation board (5);Reduction furnace (1) bottom and top are all filled with bulk drying agent (8); top end socket is provided with flange (9); nitrogen inlet (6) accesses from reduction furnace (1) top; hydrogen inlet (7) accesses from reduction furnace (1) bottom; being additionally provided with moisture analyser (10) in reduction furnace (1), the discharge nozzle (11) of reduction furnace (1) bottom accesses in the oil sump (13) equipped with protection oil (14).Reduction process nitrogen and hydrogen mixed gas, reduction process is all the time at guard catalyst;Discharge nozzle is inserted directly into below protection oil level, and not with air contact, it is good that the catalyst activity of reduction keeps;Simplify production technology, improve efficiency.

Description

Metallic catalyst reduction apparatus
Technical field
This utility model belongs to chemical equipment field, is specifically related to the reduction apparatus of a kind of metallic catalyst.
Background technology
At present in petrochemical industry or consaturated oil hydrogenation field, the nanoscale being attached on carrier all can be used Metallic catalyst, first makes oxide form by nano level metal, reduces with reduction furnace during use, and this type of reduction furnace is grasped Making complexity, safety coefficient requires high, and the metallic catalyst surfaces easily oxidation by air after reducing so that this catalyst Catalytic efficiency reduces.
Summary of the invention
The purpose of this utility model is to solve defect present in prior art, it is provided that a kind of metallic catalyst Reduction apparatus.
For achieving the above object, the technical scheme that this utility model is taked is: a kind of metallic catalyst reduction apparatus, It is characterized in that: reduction furnace (1) furnace body outer wall is provided with heat-insulation layer (4), heat-insulation layer (4) is externally provided with thermal insulation board (5);Reduction furnace (1) bottom and top are all filled with bulk drying agent (8), and top end socket is provided with flange (9), and nitrogen inlet (6) is pushed up from reduction furnace (1) Portion accesses, and hydrogen inlet (7) accesses from reduction furnace (1) bottom, is additionally provided with moisture analyser (10), reduction furnace in reduction furnace (1) (1) during the discharge nozzle (11) of bottom accesses the oil sump (13) equipped with protection oil (14).
Described heat-insulation layer (4) is by electric heating system (2) heat supply, and with the thermocouple thermometer (3) being located in reduction furnace (1) Feed back and regulate temperature.
Described oil sump (13) is provided with agitator (12), it is possible to dispersed metallic catalyst.
This utility model provides the benefit that: reduction process nitrogen and hydrogen mixed gas, and reduction process is urged in protection all the time Agent;Discharge nozzle is inserted directly into below protection oil level, and not with air contact, it is good that the catalyst activity of reduction keeps;Simplify Production technology, improves efficiency, and convenient operation, owing to the protective effect of nitrogen improves safety coefficient.
Accompanying drawing explanation
Fig. 1 is this utility model schematic diagram;
In figure: 1-reduction furnace, 2-electric heating system, 3-thermocouple thermometer, 4-heat-insulation layer, 5-thermal insulation board, 6-nitrogen enters Mouthful, 7-hydrogen inlet, 8-desiccant, 9-flange, 10-moisture analyser, 11-discharge nozzle, 12-agitator, 13-oil sump, 14-protects Protect oil.
Detailed description of the invention
Being described principle and the feature of utility model below in conjunction with accompanying drawing, example is served only for explaining that this practicality is new Type, is not intended to limit the scope of utility model.
Embodiment 1: see Fig. 1, a kind of metallic catalyst reduction apparatus, it is characterised in that: bottom reduction furnace 1 and top End socket is all filled with bulk drying agent 8, and end socket can be taken off by flange 9 and add before operation the object of needs reduction, Being passed through nitrogen by nitrogen inlet 6 before normal work and purged by the air in reduction furnace 1 clean, reduction process is simultaneously with nitrogen and hydrogen The gaseous mixture of gas does reducing atmosphere, and nitrogen inlet 6 is passed through nitrogen, is passed through hydrogen with hydrogen inlet 7, and furnace body wall is provided with electrical heating System 2, is simultaneously provided with heat-insulation layer 4 and thermal insulation board 5 ensures reduction temperature, and the reduction process moment observes the change of moisture analyser 10 Change, when not analyzing moisture, it is possible to determine that reaction in furnace terminates, close the valve before moisture analyser, close hydrogen and enter Mouth 7, slowly strengthens the valve of nitrogen inlet 6, and the nano metal after reducing with nitrogen is purged to fill guarantor by discharge nozzle 11 Protecting in the oil sump 13 of oil 14, this metallic catalyst is in the protection of nitrogen and protection oil all the time, and it is optimal that activity keeps.
Described nitrogen inlet 6 and hydrogen inlet 7 use nitrogen upper hydrogen under design, owing to density of nitrogen is more than hydrogen Air tightness so that reduction object is in nitrogen guard mode all the time, and desiccant 8 is the material that gas easily passes through.
Described electric heating system 2 feeds back with thermocouple thermometer 3 and regulates temperature.
Described oil sump 13 is provided with agitator 12 can be with dispersed metallic catalyst.
The foregoing is only standards Example of the present utility model, not in order to limit this utility model, all in this practicality Any amendment made within novel spiritual principles, equivalent, improvement etc., should be included in protection model of the present utility model Within enclosing.

Claims (3)

1. a metallic catalyst reduction apparatus, it is characterised in that: reduction furnace (1) furnace body outer wall is provided with heat-insulation layer (4), Heat-insulation layer (4) is externally provided with thermal insulation board (5);Reduction furnace (1) bottom and top are all filled with bulk drying agent (8), and top end socket is provided with Flange (9), nitrogen inlet (6) accesses from reduction furnace (1) top, and hydrogen inlet (7) accesses from reduction furnace (1) bottom, reduction furnace (1) being additionally provided with moisture analyser (10) in, the discharge nozzle (11) of reduction furnace (1) bottom accesses the oil sump equipped with protection oil (14) (13) in.
2. metallic catalyst reduction apparatus as claimed in claim 1, it is characterised in that: described heat-insulation layer (4) is added by electricity Hot systems (2) heat supply, and feed back with the thermocouple thermometer (3) being located in reduction furnace (1) and regulate temperature.
3. metallic catalyst reduction apparatus as claimed in claim 1, it is characterised in that: described oil sump (13) is provided with stirring Device (12), it is possible to dispersed metallic catalyst.
CN201620814041.9U 2016-07-31 2016-07-31 Metallic catalyst reduction apparatus Expired - Fee Related CN205850823U (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN201620814041.9U CN205850823U (en) 2016-07-31 2016-07-31 Metallic catalyst reduction apparatus

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN201620814041.9U CN205850823U (en) 2016-07-31 2016-07-31 Metallic catalyst reduction apparatus

Publications (1)

Publication Number Publication Date
CN205850823U true CN205850823U (en) 2017-01-04

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Family Applications (1)

Application Number Title Priority Date Filing Date
CN201620814041.9U Expired - Fee Related CN205850823U (en) 2016-07-31 2016-07-31 Metallic catalyst reduction apparatus

Country Status (1)

Country Link
CN (1) CN205850823U (en)

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN107634280A (en) * 2017-09-21 2018-01-26 南京分析仪器厂有限公司 The porcelain beads of CQ 1 lead to H2Restoring operation technique and its use device
CN111282518A (en) * 2018-12-10 2020-06-16 神华宁夏煤业集团有限责任公司 Method for recovering Fe-based catalyst for Fischer-Tropsch synthesis

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN107634280A (en) * 2017-09-21 2018-01-26 南京分析仪器厂有限公司 The porcelain beads of CQ 1 lead to H2Restoring operation technique and its use device
CN111282518A (en) * 2018-12-10 2020-06-16 神华宁夏煤业集团有限责任公司 Method for recovering Fe-based catalyst for Fischer-Tropsch synthesis

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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: 20170104

Termination date: 20170731