Adsorption heat pump system and cooling generation method

Patent metadata

Field	Value
Publication number	US-10168081-B2
Application number	US-201514625905-A
Country	US
Kind code	B2
Filing date	Feb 19, 2015
Priority date	Jun 30, 2014
Publication date	Jan 1, 2019
Grant date	Jan 1, 2019

Abstract

An adsorption heat pump system comprises an evaporator that evaporates an adsorbate; a first adsorption device that adsorbs the adsorbate of the evaporator and generates cooling in the evaporator; and a second adsorption device that adsorbs the adsorbate that was adsorbed by the first adsorption device and generates cooling in the first adsorption device.

First claim

What is claimed is:

1. An adsorption heat pump system comprising:
an evaporator that evaporates an adsorbate;
a plurality of first adsorption devices that adsorb the adsorbate of the evaporator and generates cooling in the evaporator, the plurality of first adsorption devices having a parallel connection that connects the plurality of first adsorption devices in parallel;
a condenser connected to the plurality of first adsorption devices via the parallel connection;
a second adsorption device that adsorbs the evaporated adsorbate from the first adsorption device through the condenser and generates cooling in the first adsorption device; and
the first adsorption device and the second adsorption device each containing a different type of adsorbent, wherein:
the adsorbent of the second adsorption device desorbs the adsorbate with heat at a higher regeneration temperature than the adsorbent of the first adsorption device, and
when an adsorption capacity of the second adsorption device is greater than an overall adsorption capacity of the plurality of first adsorption devices, the plurality of first adsorption devices are configured to adsorb the desorbed adsorbate alternatively or in sequence.

2. The adsorption heat pump system of claim 1 , wherein:
a combination of adsorbents of the first adsorption device and the second adsorption device is a combination such that, with respect to a first equilibrium pressure after the adsorbate has been desorbed by the first adsorption device, a second equilibrium pressure after the desorbed adsorbate has been absorbed by the second adsorption device is the first equilibrium pressure or lower.

3. The adsorption heat pump system of claim 1 , wherein an adsorption capacity of the second adsorption device is greater than an adsorption capacity of the first adsorption device.

4. The adsorption heat pump system of claim 1 , wherein the adsorbate is water or ammonia.

5. The adsorption heat pump system of claim 1 , wherein:
the evaporator also operates as a condenser that condenses the introduced gaseous adsorbate; and
the adsorption heat pump system further includes a bypass pipe that bypasses a plurality of the first adsorption devices and connects the evaporator and the second adsorption device together.

6. The adsorption heat pump system of claim 1 , further comprising
a plurality of the first adsorption devices that are disposed in a direction parallel to a connection direction of the evaporator and the second adsorption device.

7. The adsorption heat pump system of claim 1 , further comprising
a condenser that is provided between the first adsorption device(s) and the second adsorption device and that condenses the adsorbate.

8. A cooling generation method, using: (i) an evaporator that evaporates an adsorbate; (ii) a plurality of first adsorption devices that adsorb the adsorbate of the evaporator, the plurality of first adsorption devices having a parallel connection that connects the plurality of first adsorption devices in parallel; (ii) a condenser connected to the plurality of first adsorption devices via the parallel connection; and (iii) a second adsorption device that adsorbs the adsorbate adsorbed by the first adsorption device, the cooling generation method comprising:
adsorbing the adsorbate of the evaporator by the first adsorption device and cooling the evaporator, and
adsorbing the evaporated adsorbate of the first adsorption device by the second adsorption device through the condenser and cooling the first adsorption device, wherein:
the first adsorption device and the second adsorption device each contain a different type of adsorbent, and
the adsorbent of the second adsorption device desorbs the adsorbate with heat at a higher regeneration temperature than the adsorbent of the first adsorption device, and
when an adsorption capacity of the second adsorption device is greater than an overall adsorption capacity of the plurality of first adsorption devices, the plurality of first adsorption devices are configured to adsorb the desorbed adsorbate alternatively or in sequence.

9. The cooling generation method of claim 8 , wherein:
the evaporator also operates as a condenser that condenses the introduced gaseous adsorbate; and
the adsorbate of the second adsorption device is: (i) adsorbed by the first adsorption device, or (ii) condensed in the evaporator, during regeneration of the second adsorption device.

Assignees

• Toyota Chuo Kenkyusho Kk

Inventors

• Hirota Yasuki
• Yamauchi Takafumi
• Iwata Ryuichi
• Shimazu Takashi

Classifications

• F25B17/08 Primary

  the absorbent or adsorbent being a solid, e.g. salt (F25B17/12 takes precedence) · CPC title

• F25B17/083

  with two or more boiler-sorbers operating alternately · CPC title

• F25B30/04 Primary

  of the sorption type · CPC title

• Y02B30/62

  Absorption based systems · CPC title

• Y02B30/64

  Cross-Sectional Technologies · mapped topic