CN210419857U

CN210419857U - Energy recycling equipment for dehydrogenation work

Info

Publication number: CN210419857U
Application number: CN201920777560.6U
Authority: CN
Inventors: 范子久; 贺乾龙; 彭兴凯; 王帅; 段来阁
Original assignee: Henan Heli Energy Co ltd
Current assignee: Henan Heli Energy Co.,Ltd.
Priority date: 2019-05-28
Filing date: 2019-05-28
Publication date: 2020-04-28
Anticipated expiration: 2029-05-28

Abstract

The utility model discloses an energy recovery and recycle equipment for dehydrogenation work, including the dehydrogenation tower, cup jointed the pipe on the feed inlet of one side of dehydrogenation tower, and the dehydrogenation tower passes through pipe and liquid trap intercommunication, installs the break-make valve on the pipe, and the feed inlet of the opposite side of dehydrogenation tower passes through pipe and steam generator intercommunication, and the discharge gate of dehydrogenation tower leads to the pipe to be connected with the feed inlet of dehydrogenation condenser, and the discharge gate of dehydrogenation condenser passes through pipe and knockout intercommunication. The utility model discloses a set up cooler, biomass boiler, reduce depositing of collection ground of light component, reduce the risk of depositing safely, the light component is volatile, and is difficult for collecting the processing, through the cooler to its cooling, reduces volatilizing of light component, reduces the unorganized emission of smell, and the light component is easily fired and gives out heat very high, mixes with biomass fuel through sending to boiler pan feeding mouth, burns in the boiler, realizes the utilization of resources maximize, and the environmental protection.

Description

Energy recycling equipment for dehydrogenation work

Technical Field

The utility model relates to an energy recovery utilizes technical field, specifically is a dehydrogenation is energy recovery equipment of recycling for work.

Background

Crude oil is a complex combination mixture of various different boiling points and components. The crude oil contains light components which have lighter molecular weight and lower boiling point and are volatile, and the components are called light components and comprise naphtha, gasoline, kerosene, diesel oil and the like; the heavy components with high boiling points are called as heavy components, 150kg of light components which are generated every day in the furfural production process and 4.5 tons of light components every month are collected into a storage tank and then are stored in a leather bucket on site through data statistics, so that great potential safety hazards are caused.

The light component is flammable liquid and volatile, and can cause unorganized gas emission, produce partial smell, brought the environmental protection risk for the company, light component skin bucket storage area must keep apart because of the particularity of medium, and increases warning mark, has increased the burden for company's ann's ring meet the supervision, and light component skin bucket is collected because the change of weather, and the light component temperature of its inside storage is different, and is volatile in summer, still need consider the problem that the heat rises, increases the environmental protection risk.

SUMMERY OF THE UTILITY MODEL

Technical problem to be solved

Not enough to prior art, the utility model provides a dehydrogenation work is with energy recovery equipment of recycling, it is flammable liquid to have solved the light component, and volatile, can cause unorganized gas emission, produce partial smell, the environmental protection risk has been brought for the company, the particularity of light component skin bucket reservoir area because of the medium, must keep apart, and increase warning mark, meet the supervision and increased the burden for company's ann ring, light component skin bucket is collected because the change of weather, the light component temperature of its inside storage is different, volatile in summer, the problem that the heat rises still needs to be considered, increase the environmental protection risk.

(II) technical scheme

In order to achieve the above object, the utility model provides a following technical scheme: an energy recycling device for dehydrogenation work comprises a dehydrogenation tower, wherein a guide pipe is sleeved on a feed inlet on one side of the dehydrogenation tower, the dehydrogenation tower is communicated with a liquid collector through a guide pipe, an on-off valve is installed on the guide pipe, a feed inlet on the other side of the dehydrogenation tower is communicated with a steam generator through a guide pipe, a discharge outlet of the dehydrogenation tower is connected with a feed inlet of a dehydrogenation condenser through a guide pipe, a discharge outlet of the dehydrogenation condenser is communicated with a liquid distributor through a guide pipe, an outlet on one side of the liquid distributor is communicated with the feed inlet of the dehydrogenation tower through a guide pipe, an outlet on the other side of the liquid distributor is communicated with a feed inlet of a light component storage tank through a guide pipe, a discharge outlet of the light component storage tank is connected with a feed inlet of a high-pressure pump through a guide pipe, a discharge outlet of the high-pressure pump is connected with a feed inlet of a cooler, and the slag guide disc is arranged on a feeding port of the biomass boiler.

Preferably, the conduit is communicated with the devices at two ends of the conduit through a cut-off valve, and a steam inlet on the side wall of the dehydrogenation tower is lower than a feed inlet connected with the liquid collector of the dehydrogenation tower.

Preferably, a connecting port of the dehydrogenation tower and the dehydrogenation condenser is arranged on the outer wall above the dehydrogenation tower, and a connecting port of the liquid distributor and the dehydrogenation tower is arranged above a feeding port of the dehydrogenation tower connected with the liquid collector.

Preferably, a conduit on the discharge port of the high-pressure pump is communicated with the cooler through a stop valve, and the cooler is communicated with the stop valve through a conduit.

Preferably, the stop valve is provided with a hose through the discharge hole, and the stop valve is communicated with the slag guide disc through the hose.

(III) advantageous effects

The utility model provides a dehydrogenation is energy recovery equipment of recycling for work possesses following beneficial effect:

(1) the utility model discloses a set up cooler, biomass boiler, reduce depositing of collection ground of light component, reduce the risk of depositing safely, the light component is volatile, and is difficult for collecting the processing, through the cooler to its cooling, reduces volatilizing of light component, reduces the unorganized emission of smell, and the light component is easily fired and gives out heat very high, mixes with biomass fuel through sending to boiler pan feeding mouth, burns in the boiler, realizes the utilization of resources maximize, and the environmental protection.

(2) The utility model discloses a set up light component storage tank, pipe, on-off valve, the light component storage tank can temporarily store and defeated effect to the light component when using to avoided the too high unstable problem of direct input produced light component activity, the light component is inflammable chemicals simultaneously, need collect and sell outward, solve the problem of selling the processing outward of light component through the burning, the effectual transport to the light component of pipe and on-off valve is controlled simultaneously.

Drawings

Fig. 1 is a schematic structural view of the present invention;

fig. 2 is a flow chart of the present invention.

The reference numbers in the figures are: 1. a dehydrogenation tower; 2. a conduit; 3. an on-off valve; 4. a liquid collector; 5. a steam generator; 6. a dehydrogenation condenser; 7. a liquid separator; 8. a light component storage tank; 9. a high pressure pump; 10. a cooler; 11. a stop valve; 12. a hose; 13. a slag guide disc; 14. a biomass boiler.

Detailed Description

The technical solutions in the embodiments of the present invention will be described clearly and completely with reference to the accompanying drawings in the embodiments of the present invention, and it is obvious that the described embodiments are only some embodiments of the present invention, not all embodiments. Based on the embodiments in the present invention, all other embodiments obtained by a person skilled in the art without creative work belong to the protection scope of the present invention.

As shown in fig. 1-2, the utility model provides a technical solution: an energy recycling device for dehydrogenation work comprises a dehydrogenation tower 1, wherein a conduit 2 is sleeved on a feed inlet on one side of the dehydrogenation tower 1, the dehydrogenation tower 1 is communicated with a liquid collector 4 through the conduit 2, the conduit 2 is communicated with two-end equipment of the conduit 2 through an on-off valve 3, a steam inlet on the side wall of the dehydrogenation tower 1 is lower than a feed inlet of the dehydrogenation tower 1, which is connected with the liquid collector 4, the on-off valve 3 is installed on the conduit 2, the feed inlet on the other side of the dehydrogenation tower 1 is communicated with a steam generator 5 through the conduit 2, a discharge outlet of the dehydrogenation tower 1 is connected with a feed inlet of a dehydrogenation condenser 6 through the conduit 2, a light component storage tank 8 can temporarily store and transmit light components during use, so that the problem that the activity of the light components generated by direct input is too high and unstable is solved, meanwhile, the light components are flammable chemicals and need to be collected for sale, and the problem of light component sale treatment is, meanwhile, the guide pipe 2 and the on-off valve 3 effectively control the transportation of the light components, a connecting port of the dehydrogenation tower 1 and the dehydrogenation condenser 6 is arranged on the outer wall above the dehydrogenation tower 1, a connecting port of the liquid distributor 7 and the dehydrogenation tower 1 is arranged above a feeding port of the dehydrogenation tower 1 connected with the liquid collector 4, a discharging port of the dehydrogenation condenser 6 is communicated with the liquid distributor 7 through the guide pipe 2, an outlet at one side of the liquid distributor 7 is communicated with the feeding port of the dehydrogenation tower 1 through the guide pipe 2, an outlet at the other side of the liquid distributor 7 is communicated with a feeding port of the light components storage tank 8 through the guide pipe 2, the guide pipe 2 on the discharging port of the high-pressure pump 9 is communicated with the cooler 10 through the on-off valve 3, the cooler 10 is communicated with the stop valve 11 through the guide pipe 2, the storage of the light components in a collection place is reduced, the risk of safe storage is reduced, the light components are volatile, the volatilization of light components is reduced, the inorganization emission of odor is reduced, the light components are flammable and have high heat productivity, the light components are mixed with biomass fuel by being sent to a feeding port of a biomass boiler 14, the light components are combusted in the boiler, the resource utilization maximization is realized, and the environment is protected, a discharging port of a light component storage tank 8 is connected with a feeding port of a high-pressure pump 9 through a conduit 2, a discharging port of the high-pressure pump 9 is connected with a feeding port of a cooler 10 through the conduit 2, a hose 12 is installed on a stop valve 11 through the discharging port, the stop valve 11 is communicated with a slag guide disc 13 through the hose 12, the hose 12 is installed on the discharging port of the cooler 10, the stop valve 11 is installed on the hose 12, the tail end of the hose 12 is connected with the slag guide disc 13.

The working principle is as follows: when the device is used, the storage of a light component collecting place is reduced, the risk of safe storage is reduced, the light component is volatile and is not easy to collect and process, the temperature of the light component is reduced through a cooler, the volatilization of the light component is reduced, the unorganized emission of smell is reduced, the light component is flammable and has high heat productivity, the light component is mixed with biomass fuel through being sent to a boiler feeding hole and is combusted in a boiler, the resource utilization maximization and the environmental protection are realized, the light component can be temporarily stored and transported through a light component storage tank 8 when the device is used, the problem that the activity of the light component generated by direct input is too high and unstable is solved, meanwhile, the light component is flammable chemical and needs to be collected for sale, and the problem of light component sale processing is solved through combustion.

To sum up can, the utility model discloses a set up cooler 10, biomass boiler 14, reduce depositing of the collection ground of light component, reduce the risk of depositing safely, the light component is volatile, and is difficult for collecting the processing, cools down it through cooler 10, reduces volatilizing of light component, reduces the inorganization of smell and discharges, and the light component is easily fired and gives out heat very high, mixes with biomass fuel through sending to 14 pan feeding mouths of biomass boiler, burns in the boiler, realizes the utilization of resources maximize, and the environmental protection.

It is noted that, herein, relational terms such as first and second, and the like may be used solely to distinguish one entity or action from another entity or action without necessarily requiring or implying any actual such relationship or order between such entities or actions. Also, the terms "comprises," "comprising," or any other variation thereof, are intended to cover a non-exclusive inclusion, such that a process, method, article, or apparatus that comprises a list of elements does not include only those elements but may include other elements not expressly listed or inherent to such process, method, article, or apparatus.

Although embodiments of the present invention have been shown and described, it will be appreciated by those skilled in the art that changes, modifications, substitutions and alterations can be made in these embodiments without departing from the principles and spirit of the invention, the scope of which is defined in the appended claims and their equivalents.

Claims

1. The utility model provides an energy recovery recycles equipment for dehydrogenation work, includes dehydrogenation tower (1), its characterized in that: a guide pipe (2) is sleeved on a feed inlet on one side of a dehydrogenation tower (1), the dehydrogenation tower (1) is communicated with a liquid collector (4) through the guide pipe (2), an on-off valve (3) is installed on the guide pipe (2), the feed inlet on the other side of the dehydrogenation tower (1) is communicated with a steam generator (5) through the guide pipe (2), a discharge outlet of the dehydrogenation tower (1) is communicated with a feed inlet of a dehydrogenation condenser (6) through the guide pipe (2), a discharge outlet of the dehydrogenation condenser (6) is communicated with a liquid distributor (7) through the guide pipe (2), an outlet on one side of the liquid distributor (7) is communicated with the feed inlet of the dehydrogenation tower (1) through the guide pipe (2), an outlet on the other side of the liquid distributor (7) is communicated with a feed inlet of a light component storage tank (8) through the guide pipe (2), a discharge outlet of the light component storage tank (8) is connected with a feed inlet of a high-, the discharge port of the high-pressure pump (9) is connected with the feed inlet of the cooler (10) through the guide pipe (2), the discharge port of the cooler (10) is provided with the hose (12), the hose (12) is provided with the stop valve (11), the tail end of the hose (12) is connected with the slag guide disc (13), and the slag guide disc (13) is arranged on the feed inlet of the biomass boiler (14).

2. The apparatus according to claim 1, wherein the apparatus further comprises: the conduit (2) is communicated with devices at two ends of the conduit (2) through the on-off valve (3), and a steam inlet on the side wall of the dehydrogenation tower (1) is lower than a feed inlet for connecting the dehydrogenation tower (1) with the liquid collector (4).

3. The apparatus according to claim 1, wherein the apparatus further comprises: the connecting port of the dehydrogenation tower (1) and the dehydrogenation condenser (6) is arranged on the outer wall above the dehydrogenation tower (1), and the connecting port of the liquid distributor (7) and the dehydrogenation tower (1) is arranged above the feeding port of the dehydrogenation tower (1) connected with the liquid collector (4).

4. The apparatus according to claim 1, wherein the apparatus further comprises: a guide pipe (2) on a discharge port of the high-pressure pump (9) is communicated with a cooler (10) through a cut-off valve (3), and the cooler (10) is communicated with a stop valve (11) through the guide pipe (2).

5. The apparatus according to claim 1, wherein the apparatus further comprises: the stop valve (11) is provided with a hose (12) through a discharge hole, and the stop valve (11) is communicated with the slag guide disc (13) through the hose (12).