CN205948867U - High pressure circulation reaction unit - Google Patents
High pressure circulation reaction unit Download PDFInfo
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- CN205948867U CN205948867U CN201621026500.3U CN201621026500U CN205948867U CN 205948867 U CN205948867 U CN 205948867U CN 201621026500 U CN201621026500 U CN 201621026500U CN 205948867 U CN205948867 U CN 205948867U
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Abstract
The utility model discloses a high pressure circulation reaction unit, including admission valve (1), filter (2), surge damping valve (3), manifold pressure gage (4), flowmeter (5), reactor (6), condenser (7), separator (8), drainage valve (9), system pressure table (10), back pressure valve (11), booster pump (12), head tank admission valve (13), head tank manometer (14), head tank (15) and atmospheric valve (16). The utility model has the advantages that: reasonable in design, overall arrangement be compact, can realize tail gas recycling etc.
Description
Technical field:
The utility model is related to a kind of cycle of higher pressure reaction unit, belongs to technical field of chemical.
Background technology:
There is a class hydrogenation reaction device, high-pressure hydrogenation and other high pressure for liquid material are anti-in chemical engineering experiment device
Should, for Fast Evaluation and screening catalyst, determine preliminary process conditions, be needs for reacted hydrogen in this kind of device
It is circulated reaction.Based on case above it is necessary to develop band circulation High-pressure Hydrogenation Unit, for catalytic hydrogenation, catalysis
The courses of reaction such as cracking, disproportionation.
Content of the invention:
Technical problem to be solved in the utility model is to provide a kind of reasonable in design, compact in design, enable tail gas and follow
The cycle of higher pressure reaction unit of ring.
Cycle of higher pressure reaction unit described in the utility model, including intake valve (1), filter (2), pressure maintaining valve (3), air inlet
Pressure gauge (4), flowmeter (5), reactor (6), condenser (7), separator (8), bleeder valve (9), system pressure table (10), the back of the body
Pressure valve (11), booster pump (12), head tank intake valve (13), head tank pressure gauge (14), head tank (15) and atmospheric valve (16),
It is characterized in that:Described head tank (15) top successively with intake valve (1), filter (2), pressure maintaining valve (3), flowmeter (5),
Reactor (6), condenser (7), 1 end of separator (8) are connected, and the entrance of described flowmeter (5) is connected with boost gauge
(4), 3 ends of described separator (8) are connected with bleeder valve (9), and 2 ends of separator (8) are connected with the entrance of counterbalance valve (11),
The described entrance of counterbalance valve (11) is connected with system pressure table (11), the outlet of counterbalance valve (11) and booster pump (12) entrance phase
Even, described booster pump (12) outlet is connected with head tank (15), and the bottom of described head tank (15) is connected with atmospheric valve
(16), the top of head tank (15) is connected with head tank pressure gauge (14) and head tank intake valve (13).
The beneficial effects of the utility model are:Reasonable in design, compact in design, the circulation being capable of reaction end gas is anti-
Should, easy to use.
Brief description:
Fig. 1 is cycle of higher pressure reaction unit structural representation.
Specific embodiment:
Below in conjunction with the accompanying drawings the utility model is described in further detail;
Cycle of higher pressure reaction unit as shown in Figure 1, by intake valve (1), filter (2), pressure maintaining valve (3), boost gauge
(4), flowmeter (5), reactor (6), condenser (7), separator (8), bleeder valve (9), system pressure table (10), counterbalance valve
(11), booster pump (12), head tank intake valve (13), head tank pressure gauge (14), head tank (15) and atmospheric valve (16) composition,
Head tank (15) top successively with intake valve (1), filter (2), pressure maintaining valve (3), flowmeter (5), reactor (6), condenser
(7), 1 end of separator (8) is connected, and the entrance of flowmeter (5) is connected with boost gauge (4), 3 ends of separator (8) with put
Liquid valve (9) is connected, and 2 ends of separator (8) are connected with the entrance of counterbalance valve (11), the entrance of counterbalance valve (11) and system pressure table
(11) it is connected, the outlet of counterbalance valve (11) is connected with booster pump (12) entrance, booster pump (12) outlet is connected with head tank (15),
The bottom of head tank (15) is connected with atmospheric valve (16), and the top of head tank (15) is connected with head tank pressure gauge (14) and raw material
Canister incoming gas valve (13).
Here the utility model description and application are illustrative, are not wishing to be limited in scope of the present utility model above-mentioned
In embodiment, therefore, the utility model is not limited by the present embodiment, and the technical scheme that any employing equivalence replacement obtains all exists
In the range of the utility model protection.
Claims (1)
1. cycle of higher pressure reaction unit, including intake valve (1), filter (2), pressure maintaining valve (3), boost gauge (4), flowmeter
(5), reactor (6), condenser (7), separator (8), bleeder valve (9), system pressure table (10), counterbalance valve (11), booster pump
(12), head tank intake valve (13), head tank pressure gauge (14), head tank (15) and atmospheric valve (16) it is characterised in that:Described
Head tank (15) top successively with intake valve (1), filter (2), pressure maintaining valve (3), flowmeter (5), reactor (6), condensation
Device (7), 1 end of separator (8) are connected, and the entrance of described flowmeter (5) is connected with boost gauge (4), described separation
3 ends of device (8) are connected with bleeder valve (9), and 2 ends of separator (8) are connected with the entrance of counterbalance valve (11), described counterbalance valve
(11) entrance is connected with system pressure table (10), and the outlet of counterbalance valve (11) is connected with booster pump (12) entrance, described increasing
Press pump (12) outlet is connected with head tank (15), and the bottom of described head tank (15) is connected with atmospheric valve (16), head tank
(15) top is connected with head tank pressure gauge (14) and head tank intake valve (13).
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
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CN201621026500.3U CN205948867U (en) | 2016-08-25 | 2016-08-25 | High pressure circulation reaction unit |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
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CN201621026500.3U CN205948867U (en) | 2016-08-25 | 2016-08-25 | High pressure circulation reaction unit |
Publications (1)
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CN205948867U true CN205948867U (en) | 2017-02-15 |
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CN201621026500.3U Active CN205948867U (en) | 2016-08-25 | 2016-08-25 | High pressure circulation reaction unit |
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CN (1) | CN205948867U (en) |
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN112129852A (en) * | 2020-08-31 | 2020-12-25 | 中国科学院福建物质结构研究所 | Reaction gas cyclic utilization and controllable CO dehydrogenation of atmosphere purifies catalyst evaluation device |
-
2016
- 2016-08-25 CN CN201621026500.3U patent/CN205948867U/en active Active
Cited By (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN112129852A (en) * | 2020-08-31 | 2020-12-25 | 中国科学院福建物质结构研究所 | Reaction gas cyclic utilization and controllable CO dehydrogenation of atmosphere purifies catalyst evaluation device |
CN112129852B (en) * | 2020-08-31 | 2021-08-10 | 中国科学院福建物质结构研究所 | Reaction gas cyclic utilization and controllable CO dehydrogenation of atmosphere purifies catalyst evaluation device |
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