• Tidak ada hasil yang ditemukan

การลดการระเหยของน้ำร้อนในกระบวนการผลิตผลไม้กระป๋อง

N/A
N/A
Protected

Academic year: 2023

Membagikan "การลดการระเหยของน้ำร้อนในกระบวนการผลิตผลไม้กระป๋อง"

Copied!
5
0
0

Teks penuh

(1)

„µ¦¨—„µ¦¦³Á®¥…°ŠœÊε¦o°œÄœ„¦³ªœ„µ¦Ÿ¨·˜Ÿ¨Å¤o„¦³žl°Š

The reduction of vaporization of boiling water in the fruit canning process

°£·¦´„¬r ­ª´­—·Í„·‹

1*

š¸ž„¦ ‡»–µ¡¦ª·ª´•œr

1

‹´„¦¡´œ›r „´–®µ

1

¨³ ª¦¡‹œr ¡´œ›»r‡Š

1

£µ‡ª·µª·«ª„¦¦¤Á‡¦ºÉ°Š„¨ ‡–³ª·«ª„¦¦¤«µ­˜¦r ¤®µª·š¥µ¨´¥«¦¸žš»¤ 61 ™œœ¡®¨Ã¥›·œ

Á…˜‹˜»‹´„¦ „¦»ŠÁš¡² 10900 Ú¦ 02-5791111 Ú¦­µ¦ 02-5611721 *E-mail: apirak@spu.ac.th

2

£µ‡ª·µª·«ª„¦¦¤°»˜­µ®„µ¦ ‡–³ª·«ª„¦¦¤«µ­˜¦r ¤®µª·š¥µ¨´¥«¦¸žš»¤ 61 ™œœ¡®¨Ã¥›·œ

Á…˜‹˜»‹´„¦ „¦»ŠÁš¡² 10900 Ú¦ 02-5791111 Ú¦­µ¦ 02-5611721 E-mail: worapoj@spu.ac.th

apirak sawadkit

1*

, teapagon counaphonwiwat

1

, jagapan gunha

1

, and worapoj phankong

2

1

Department of Mechanical Engineering, Faculty of Engineering, Sripatum University

61 Phaholyothin Rd., Jatujak, Bangkok 10900 Tel : 02-5791111, Fax : 02-5611721 *E-mail: apirak@spu.ac.th

2

Department of lndustrial Engineering, Faculty of Engineering, Sripatum University

61 Phaholyothin Rd., Jatujak, Bangkok 10900 Tel : 02-5791111, Fax : 02-5611721 E-mail: worapoj@spu.ac.th

š‡´—¥n°

š‡ªµ¤œ¸Ê Áž}œ„µ¦«¹„¬µ¤µ˜¦„µ¦ž¦³®¥´—Å°œÊε×¥„µ¦¨—„µ¦

¦³Á®¥…°ŠœÊε¦o°œÄœ°»ž„¦–rš¸ÉčoĜ„µ¦˜o¤°‰nµÁºÊ°Ÿ¨·˜£´–”r…°Š

„¦³ªœ„µ¦Ÿ¨·˜Ÿ¨Å¤o„¦³žl°ŠÄœÃ¦ŠŠµœÂ®nŠ®œ¹ÉŠ Ž¹ÉŠÄo­´ž³¦—Áž}œ

ª´˜™»—·®¨´„ ¤¸„ε¨´Š„µ¦Ÿ¨·˜ÁŒ¨¸É¥ 150,000 ˜´œ˜n°že šÎµŠµœ 2,504

´ÉªÃ¤Š˜n°že …´Êœ˜°œÁ¦·É¤‹µ„„µ¦«¹„¬µŸ¨„µ¦ª·Á‡¦µ³®r¡¨´ŠŠµœ…°Š

Á‡¦ºÉ°Š°‰nµÁºÊ°Ž¹ÉŠ¤¸¨´„¬–³Áž}œ™´Šš¦ŠÁ®¨¸É¥¤šÎµ—oª¥Â˜œÁ¨­ …œµ—

„ªoµŠ 1.62 Á¤˜¦ ¥µª 7.32 Á¤˜¦ ¨³­¼Š 0.34 Á¤˜¦ čoÅ°œÊε°·É¤˜´ª

‡ªµ¤—´œ 1.0 µ¦r ž¦·¤µ–ÁŒ¨¸É¥ 80 „·Ã¨„¦´¤˜n°´ÉªÃ¤Š ž¦³­·š›·£µ¡

Á‡¦ºÉ°Š²Ášnµ„´ 36.43% ¤µ˜¦„µ¦ž¦³®¥´—Å°œÊεš¸Éčo¤¸ 2 ¤µ˜¦„µ¦‡º°

„µ¦¨—°´˜¦µ„µ¦™nµ¥Áš‡ªµ¤¦o°œš¸ÉŸœ´Š™´ŠÃ—¥Äo­µ¦ nunsulate šµ Á‡¨º°š¸ÉŸ·ª—oµœœ°„…°ŠŸœ´ŠÁ‡¦ºÉ°Š² °´˜¦µŸ¨˜°Âšœ„µ¦¨Šš»œ…°Š

¤µ˜¦„µ¦ 218% ¦³¥³Áª¨µ‡ºœš»œ 0.5 že ­Îµ®¦´¤µ˜¦„µ¦¨—„µ¦

¦³Á®¥…°ŠœÊε¦o°œÃ—¥Äo¨¼„°¨š¦Š„¨¤š¸ÉšÎµ‹µ„¡¨µ­˜·„ž¦³Á£š

polycarbonate ¨°¥žd—Ÿ·ªÁ¡ºÉ°¨—„µ¦¦³Á®¥…°Š‡ªµ¤¦o°œš¸ÉŸ·ªœÊε

°´˜¦µŸ¨˜°Âšœ„µ¦¨Šš»œ…°Š¤µ˜¦„µ¦Ášnµ„´ 91.82% ¦³¥³Áª¨µ

‡ºœš»œ 1.19 že ¨³‹µ„¤µ˜¦„µ¦š´ÊŠ­°ŠšÎµÄ®ož¦³­·š›·£µ¡Á‡¦ºÉ°Š² Á¡·É¤…¹ÊœÁž}œ 44.41% ‡·—Áž}œÅ°œÊεš¸Éž¦³®¥´—Å—o 17.95%

‡Îµ­Îµ‡´ : „µ¦¦³Á®¥ / Á‡¦ºÉ°Š°‰nµÁºÊ° / Ÿ¨Å¤o„¦³žl°Š / ­¤—»¨

¡¨´ŠŠµœ / „µ¦ž¦³®¥´—Å°œÊε Abstract

This research aimed to study vapor saving measure by reducing the vaporization of boiling water used for sterilization in

fruit canning process in a pineapple-processed factory with an average productivity of 150,000 tons and 2,504 working hours per year. The study began with the energy analysis of the sterilizer machine which is a stainless rectangular tank, 1.62 meters wide, 7.32 meters long, and 0.34 meters high, using 1.0 bar saturated vapor pressure, averagely 80 kilograms per hour, and working at 36.43% performance. A vapor saving measures used was the reduction of heat transfer via the tank wall by coating the outer wall with nunsulate chemical. This measure provided 218 % return on investment within 0.5 year payback period. Another measure was the use of a round plastic ball made of polycarbonate floating over the surface to reduce the vaporization of boiling water through water surface. This measure provided 91.82% return on investment within 1.19 year payback period.

Both measures increased 44.41% machine performance and saved 17.95% vapor.

Keywords : vapouring / sterilizer machine / canned fruit / energy balance / steam conservation

1.šœÎµ

°»˜­µ®„¦¦¤„µ¦Ÿ¨·˜Ã—¥š´ÉªÅž Ťnªnµ‹³Áž}œ°»˜­µ®„¦¦¤­·ÉŠš°

°µ®µ¦ Á‡¦ºÉ°Š°»žÃ£‡¦·Ã£‡ ²¨² ¤´„°µ«´¥‡ªµ¤¦o°œ‹µ„Å°œÊεÁ¡ºÉ°Äo Ĝ„¦³ªœ„µ¦Ÿ¨·˜ „µ¦˜¦ª‹­°Îµ¦»Š¦´„¬µ¦ª¤š´ÊŠŽn°¤ÂŽ¤

°»ž„¦–r˜nµŠ Ç š¸ÉčoĜ¦³Å°œÊε°¥nµŠ­¤ÉεÁ­¤° œ°„‹µ„‹³šÎµÄ®o 18 20 ˜»¨µ‡¤ 2549 ‹Š®ª—œ‡¦¦µ­¤µ ETM041

(2)

ž¦³­·š›·£µ¡Á·Š‡ªµ¤¦o°œ…°Š¦³—¸…¹ÊœÂ¨oª¥´Š­µ¤µ¦™ž¦³®¥´—Å°œÊε ¨³ÁºÊ°Á¡¨·Šš¸Éčoŗo—´Šš¸É­—ŠÄœ [1,2]

Ĝ„µ¦«¹„¬µÅ—oÁ¨º°„Á°µ„¦³ªœ„µ¦Ÿ¨·˜Ÿ¨Å¤o„¦³žl°ŠŽ¹ÉŠ¤¸„µ¦

čo Å°œÊεĜ„¦³ªœ„µ¦°‰nµÁºÊ°Ÿ¨·˜£´–”r®¦º°­´ž³¦—„¦³žl°Š

×¥°µ«´¥„¦¦¤ª·›¸˜nµŠ Ç š¸É­µ¤µ¦™šÎµÅ—o¨³Å¤n„¦³š„´„¦³ªœ„µ¦

Ÿ¨·˜Â¨³˜´ªŸ¨·˜£´–”r ×¥°µ«´¥Ÿ¨„µ¦„µ¦­¤—»¨‡ªµ¤¦o°œ…°Š

Á‡¦ºÉ°Š‹´„¦Á¡ºÉ°—¼„µ¦­¼Á­¸¥š¸ÉÁ„·—…¹Êœ‹µ„œ´Êœ‹¹ŠÁ¨º°„čo¤µ˜¦„µ¦š¸É¤¸

Ÿ¨„¦³š„´„¦³ªœ„µ¦Ÿ¨·˜œo°¥­»—Á¡ºÉ°šÎµÄ®oÁ„·—„µ¦ž¦³®¥´—Å°œÊε

Ÿ¨š¸Éŗo‹µ„ǦŠ„µ¦œ¸Ê ­µ¤µ¦™œÎµÅžÄo„´„¨»n¤°»˜­µ®„¦¦¤®¦º°

Á„¬˜¦„¦¦¤°ºÉœÇ š¸É¤¸¨´„¬–³„µ¦Äo¡¨´ŠŠµœÄœÁ‡¦ºÉ°Š‹´„¦š¸É¤¸¦¼žÂ

„µ¦šÎµŠµœÄ„¨oÁ‡¸¥Š„´œ

¦¼žš¸É 1 ŸœŸ´Š„µ¦Ÿ¨·˜­´ž³¦—„¦³žl°Š

2.…´Êœ˜°œ„µ¦Ÿ¨·˜­´ž³¦—„¦³žl°Š

­´ž³¦—™¼„¨ÎµÁ¨¸¥ŠÁ…oµ­¼nŸœ„¦´ª´˜™»—·Â¨³­nŠÁ…oµ¦³ ×¥

screw grader Á¡ºÉ°šÎµ„µ¦‡´—Â¥„…œµ— ¦ª¤š´ÊŠ˜¦ª‹­°šµŠ

„µ¥£µ¡Â¨³‹³™¼„¨ÎµÁ¨¸¥ŠŸnµœn°œÊε¦o°œ š¸É¤¸‡¨°¦¸œŸ­¤°¥¼nÁ¡ºÉ°³¨oµŠ

šÎµ‡ªµ¤­³°µ— ‹µ„œ´Êœ‹³™¼„­nŠÁ…oµ­¼n„¦³ªœ„µ¦˜´—®´ªšoµ¥ ¨oªž°„

Áž¨º°„—oª¥Á‡¦ºÉ°Š ginaca š¸É­µ¤µ¦™ž¦´Â˜nŠ¦³¥³…°ŠÄ¤¸—Ä®o

¡°Á®¤µ³„´…œµ—…°ŠŸ¨­´ž³¦—Ťn®œµ®¦º°µŠÁ„·œÅž µŠ‡¦´ÊŠ

°µ‹¤¸Á«¬…°Š˜µ­´ž³¦—˜·—°¥¼nš¸ÉŸ¨®¨´Š„µ¦ž°„Áž¨º°„„È‹³¤¸¡œ´„Šµœ

š¸É‡°¥˜¦ª‹­°‹·„˜µ°°„‹œ®¤— ¨³œÎµÅž¨oµŠšÎµ‡ªµ¤­³°µ—°¸„

‡¦´ÊŠ ‹µ„œ´Êœ­´ž³¦—‹³™¼„˜´—°°„Áž}œÂªnœ˜µ¤‡ªµ¤®œµš¸É„ε®œ—

…¹Êœ°¥¼n„´…œµ—„¦³žl°Šš¸É¦¦‹» Ž¹ÉŠ¤¸…œµ— 20, 30 ¨³ 108 OZ. Á¤ºÉ°

­´ž³¦—™¼„˜´—Áž}œÂªnœÂ¨oª‹³™¼„Á‹µ³Â„œ Á­¦È‹Â¨oª‹¹ŠœÎµÁ…oµ¦³

¦¦‹»„¦³žl°Š—oª¥Á‡¦ºÉ°Š can loader ¨³Á˜·¤œÊεÁºÉ°¤¨ŠÄœ„¦³žl°ŠÁ¡ºÉ°

‡ª‡»¤‡»–£µ¡Â¨³¦­µ—Ä®oÁž}œÅž˜µ¤‡ªµ¤˜o°Š„µ¦ „¦³ªœ„µ¦

¦¦‹»ÁœºÊ°­´ž³¦—¨³œÊεÁºÉ°¤œ¸Ê ‹³°¥¼n£µ¥Ä˜o‡ªµ¤˜o°Š„µ¦…°Š¨¼„‡oµ ªnµ­´—­nªœ…°ŠÁœºÊ°­´ž³¦—„´œÊεÁºÉ°¤Áž}œÁšnµÅ¦ ®¨´Š„µ¦Á˜·¤œÊεÁºÉ°¤

‹³Ÿnµœ„¦¦¤ª·›¸šµŠ‡ªµ¤¦o°œÁ¡ºÉ°Å¨n¢°Š°µ„µ«Ã—¥Á‡¦ºÉ°Š exhaust box¨³™¼„­nŠŸnµœ­µ¥¡µœ¨ÎµÁ¨¸¥ŠÅž¥´ŠÁ‡¦ºÉ°Š seamer Á¡ºÉ°šÎµ„µ¦

žd— µ®¨´Š‹µ„œ´Êœ‹¹Š­nŠÅž¥´ŠÁ‡¦ºÉ°Š°‰nµÁºÊ° (cooker) ŸœŸ´Š…´Êœ˜°œ

„µ¦Ÿ¨·˜Â­—ŠÄœ¦¼žš¸É 1

¨´„¬–³„µ¦Ÿ¨·˜Â¨³ÄoÅ°œÊεĜ„¦³ªœ„µ¦Ÿ¨·˜…°ŠÃ¦ŠŠµœ Ž¹ÉŠ

ŗo‹µ„®¤o°Å°œÊεš¸É¤¸¡·„´— 16 µ¦r 14 ˜´œ/´ÉªÃ¤Š Áž}œœ·—Å°°·É¤˜´ª¤¸

‡ªµ¤—´œÄoŠµœ 12 µ¦r Å°œÊεš¸ÉŸ¨·˜Å—o‹³™¼„­nŠŸnµœÅžÄœ¦³šn°­nŠ

Å°œÊεŸnµœªµ¨rª¨—‡ªµ¤—´œ (Reducing valve) Á¡ºÉ°Ä®oŗo‡ªµ¤—´œ

Ášnµ„´‡ªµ¤˜o°Š„µ¦…°ŠÁ‡¦ºÉ°Š‹´„¦œ´Êœ Ç Å°œÊεš¸É Ÿ¨·˜‹³™¼„Â¥„

°°„Áž}œ 2 ­nªœ ‡º°­nªœ…°ŠÁ‡¦ºÉ°Š°‰nµÁºÊ°Â¨³„¦³ªœ„µ¦Ÿ¨·˜

°ºÉœ Ç œÊε¤´œÁºÊ°Á¡¨·Šš¸Éčo„´®¤o°Å°œÊεÁž}œœÊε¤´œÁ˜µÁ„¦—Ž¸ ¦µ‡µ 11.50µš/¨·˜¦ ¤¸‡nµ‡ªµ¤¦o°œ­¼Š (HHV) 39,893 „·Ã¨‹¼¨/¨·˜¦ ¦¼žš¸É 2 ­—ŠÄ®oÁ®Èœ™¹ŠÂŸœŸ´Š„µ¦Ÿ¨·˜Â¨³­nŠ‹nµ¥Å°œÊεĮo„´„¦³ªœ„µ¦°

‰nµÁºÊ°ÄœÃ¦ŠŠµœ

3.„¦¦¤ª·›¸„µ¦«¹„¬µ

Á‡¦ºÉ°Š‹´„¦š¸Éčo Ĝ„µ¦Á‡¦ºÉ°Š°‰nµÁºÊ°¤¸¨´„¬–³Áž}œ°nµŠ¦¦‹»œÊε

¦o°œ‹Îµœªœ­°Š´Êœ ˜n¨³´Êœ„ªoµŠ 1.62 m ¥µª 7.32 m ¨³­¼Š 0.34 m čoÅ°œÊε°·É¤˜´ª‡ªµ¤—´œ 1.0 bar.g ž¦·¤µ–ÁŒ¨¸É¥ 80 kg/hr °»–®£¼¤·œÊε

¦o°œš¸ÉčoĜ„µ¦˜o¤Ÿ¨·˜£´–”rž¦³¤µ– 97 – 99 ÑC ‹µ„¨´„¬–³„µ¦

čoŠµœ¡ªnµ ¤¸„µ¦­¼Á­¸¥‡ªµ¤¦o°œ°°„‹µ„˜´ªÁ‡¦ºÉ°Š®¨µ¥š·«šµŠŽ¹ÉŠ

ŗošÎµ„µ¦˜¦ª‹ª´—Á¡ºÉ°­¤—»¨‡ªµ¤¦o°œ ¨³®µ¤µ˜¦„µ¦Äœ„µ¦ž¦³®¥´—

×¥¤¸¨³Á°¸¥——´Šœ¸Ê

3.1„µ¦ª·Á‡¦µ³®r‡ªµ¤¦o°œ­¼Á­¸¥

„µ¦ª·Á‡¦µ³®r¤ª¨ ¨³‡ªµ¤¦o°œš¸É™nµ¥ÁšÁ…oµÂ¨³°°„‹µ„¦³

˜µ¤¨´„¬–³…°ŠÁ‡¦ºÉ°Š°‰nµÁºÊ°š¸É­—Š°¥¼nĜ¦¼žš¸É 3 œ´Êœ„µ¦ª·Á‡¦µ³®r

°µ«´¥…o°¤¼¨š¸Éŗo‹µ„„µ¦˜¦ª‹ª´—‡»–­¤´˜·˜nµŠ Ç ‹¦·Š˜µ¤­£µª³„µ¦

šÎµŠµœÁnœž¦·¤µ–Å°œÊεš¸Éčo °»–®£¼¤· ‡ªµ¤—´œ ²¨² œ°„‹µ„œ´Êœ¥´Š

°µ«´¥…o°¤¼¨‹µ„Á°„­µ¦¦ª¤š´ÊŠ­¤¤˜·“µœ˜nµŠ Ç š¸Éŗo„ε®œ—…¹Êœ ×¥¤¸

¦µ¥¨³Á°¸¥—…°Š„µ¦«¹„¬µ—´Šœ¸Ê

Ÿ¨­´ž³¦—

¨oµŠšÎµ‡ªµ¤­³°µ——oª¥œÊ娳‡¨°¦¸œ (Washing)

ž°„Áž¨º°„ (Pelling by Ginaca)

˜´—Áž}œÂªnœ(Slicing)

Á‹µ³Â„œ (Punching)

¦¦‹»„¦³žl°Š(Filling)

¦¦‹»¨Š®¸(Packing)

‡´—Â¥„ (Grading)

Á˜·¤œÊεÁºÉ°¤(Syruping)

°‰nµÁºÊ°(Sterilizing) Ũn¢°Š°µ„µ«(Exhausting)

„µ¦ž¦³»¤ª·µ„µ¦Á‡¦º°…nµ¥ª·«ª„¦¦¤Á‡¦ºÉ°Š„¨Â®nŠž¦³Áš«Åš¥‡¦´ÊŠš¸É 20 18-20 ˜»¨µ‡¤ 2549 ‹´Š®ª´—œ‡¦¦µ­¸¤µ

Suranaree University of Technology

ETM041

18-20 October 2006 , Mandarin Golden Valley Hotel & Resort Khao Yai , Nakhon Ratchasima

(3)

¦¼žš¸É 2 ŸœŸ´Š„µ¦Ÿ¨·˜Â¨³ÄoÅ°œÊε…°ŠÃ¦ŠŠµœ

3.1.1 ­¤„µ¦š¸ÉčoĜ„µ¦ª·Á‡¦µ³®r ž¦³„°Åž—oª¥ [2,3]

1. „µ¦­¤—»¨¤ª¨…°Š¦³

mv = ms (1)

×¥š¸É mv ‡º° ¤ª¨…°ŠœÊ妳Á®¥ ms‡º° ¤ª¨Å°œÊεÁ…oµ¦³

2. ‡ªµ¤¦o°œ‹µ„Å°œÊε

QÅ°œÊε = ms hg (2) ×¥š¸É hg‡º° Á°œ›´¨žeÅ°œÊε…µÁ…oµ

3.‡ªµ¤¦o°œ‹µ„Ÿ¨·˜£´–”r

QŸ¨·˜£´–”r= mp Cp'T (3) ×¥š¸É mp ‡º° ¤ª¨Ÿ¨·˜£´–”rš¸ÉÁ…oµ Cp ‡º° ‡ªµ¤¦o°œ‹ÎµÁ¡µ³…°Š

­´ž³¦—­nªœš¸ÉÁž}œÁœºÊ°(1.7166 kJ/kg) 'T ‡º° Ÿ¨˜nµŠ…°Š°»–®£¼¤·

Ÿ¨·˜£´–”rÁ…oµ°°„

4. ‡ªµ¤¦o°œ‹µ„œÊεš¸É¦³Á®¥

QœÊ妳Á®¥= mv hg (4) ×¥š¸É hg‡º° Á°œ›´¨že…°ŠœÊ妳Á®¥

5.‡ªµ¤¦o°œ­¼Á­¸¥°°„‹µ„Ÿœ´Š™´Š [4] Á„·—‹µ„„µ¦™nµ¥Áš°°„

‹µ„Ÿ·ªŸœ´ŠÃ—¥„µ¦¡µ‡ªµ¤¦o°œ ¨³„µ¦ÂŸn¦´Š­¸‡ªµ¤¦o°œ­¼n¦¦¥µ„µ«

—´Šœ¸Ê

„µ¦­¼Á­¸¥‡ªµ¤¦o°œÃ—¥„µ¦¡µ‡ªµ¤¦o°œ

QCV= h A (TS-Tf) (5) ×¥š¸É h‡º° ­´¤ž¦³­·š›·Í„µ¦¡µ‡ªµ¤¦o°œÂ›¦¦¤µ˜· A‡º° ¡ºÊœš¸É

Ÿ·ª™nµ¥Áš‡ªµ¤¦o°œ (‹µ„…œµ—¤·˜·…°ŠÁ‡¦ºÉ°Š) TS ‡º° °»–®£¼¤·Ÿ·ª

Ÿœ´Š™´Š Tf ‡º°°»–®£¼¤·¦¦¥µ„µ«¦·Áª–把µœ

‡nµ­´¤ž¦³­·š›·Í„µ¦¡µ‡ªµ¤¦o°œ‡Îµœª–˜µ¤­¤„µ¦

L k

h NuL (6)

×¥š¸É NuL ‡º° œ´­ÁŽ¨šrœ´¤Á°¦r (Nusselt number) ­Îµ®¦´„¦–¸œ¸Ê

°»–®£¼¤·Ÿœ´ŠÂŸnœÁ¦¸¥‹³¤¸‡nµ‡Šš¸É¨³ÂŸnœÁ¦¸¥ªµŠÄœÂœª—·ÉŠ k ‡º°

‡ªµ¤­µ¤µ¦™„µ¦œÎµ‡ªµ¤¦o°œ…°Š°µ„µ« L ‡º° ‡ªµ¤­¼ŠŸœ´Š¦µªµŠ

Ĝœª—·ÉŠ…°ŠÁ‡¦ºÉ°Š°‰nµÁºÊ°

‡nµœ´­ÁŽ¨šrœ´¤Á°¦r ­Îµ®¦´Ÿœ´ŠÂœª˜´ÊŠ…°ŠÁ‡¦ºÉ°Š²‡Îµœª–Å—o

‹µ„­¤„µ¦š¸É (7) Ž¹ÉŠÄoŗo„´¨´„¬–³„µ¦Å®¨…°Š°µ„µ«š¸ÉŸnµœŸœ´Šš´ÊŠ

18-20 ˜»¨µ‡¤ 2549 ‹´Š®ª´—œ‡¦¦µ­¸¤µ ETM041

(4)

„µ¦Å®¨š¸ÉÁž}œÂ¨µ¦r¤·œµ¦r¨³Áš°¦r·ªÁ¨œšr ®¦º° 10-1<RaL<1012 Á¤ºÉ° RaL‡º° Á¦¥rÁ¨¥rœ´¤Á°¦r (Rayleigh number)

2

°¿

°¾

½

°¯

°®

­

9/16 8/27

1/6

] /Pr) (

[

LPr) L Gr

Nu 1 0.492

0.387

0.825 (

(7)

×¥š¸É Pr‡º° ¡¦oµœšrœ´¤Á°¦r (Prandtl number) ¨³ GrL‡º° „¦r

°¡œ´¤Á°¦r (Grashof number) ‡Îµœª–‹µ„­¤„µ¦

2 3

Ȟ )L T ȕ(T L g

Gr s f

(8)

„µ¦­¼Á­¸¥‡ªµ¤¦o°œÃ—¥„µ¦ÂŸn¦´Š­¸‡ªµ¤¦o°œ

QRA = V H A (TS4-Tf4) (9) ×¥š¸É V ‡º° ‡nµ‡Šš¸É…°Š­Á˜¢µœÂ¨³Ã¨Žr¤œ (5.67u10-8W/m2.K4)

H ‡º° Emittance …°ŠŸ·ªÁ‡¦ºÉ°Š‹´„¦Ášnµ„´ 0.7 [4]

„µ¦­¼Á­¸¥‡ªµ¤¦o°œ¦ª¤š¸É°°„‹µ„Ÿœ´Š

QŸnµœŸœ´Š= QCV+QRA (10)

6. „µ¦­¼Á­¸¥‡ªµ¤¦o°œ°ºÉœ Ç ‹³¤¸°Š‡rž¦³„°®¨µ¥­nªœ Ž¹ÉŠ

Ťn­µ¤µ¦™®¨¸„Á¨¸É¥Š®¦º°Â„oŅŗo Ánœ „µ¦°¤‡ªµ¤¦o°œ‹µ„˜´ª Á‡¦ºÉ°Š‹´„¦­nªœš¸ÉÁž}œÃ¨®³ ¦³­µ¥¡µœ¨ÎµÁ¨¸¥ „µ¦™nµ¥Áš‡ªµ¤¦o°œ

š¸É„oœ™´ŠœÊε¦o°œ ²¨² ˜n„Ȥ¸‡nµÅ¤n¤µ„œ´„Á¤ºÉ°Áš¸¥„´Áš°¤°ºÉœ Ç 7. „µ¦­¤—»¨‡ªµ¤¦o°œ ‹µ„„¦¦¤ª·›¸Â¨³Äo­¤„µ¦…oµŠ˜oœ­µ¤µ¦™

­¤—»¨¦³Å—o˜µ¤­¤„µ¦š¸É(11) š·«šµŠ„µ¦™nµ¥Áš‡ªµ¤¦o°œÄœ¦³

­—ŠÄœ¦¼žš¸É 3

QÅ°œÊε= QŸ¨·˜£´–”r+Q¦³Á®¥+QŸnµœŸœ´Š+Q°ºÉœ Ç (11) 3.1.2 ž¦³­·š›·£µ¡Á·Š‡ªµ¤¦o°œ…°ŠÁ‡¦ºÉ°Š°‰nµÁºÊ° (Kcooker) ×¥

¡·‹µ¦–µ„µ„‡ªµ¤¦o°œš¸ÉŸ¨·˜£´–”rŗo¦´˜n°‡ªµ¤¦o°œš¸Éčoš´ÊŠ®¤—˜µ¤

­¤„µ¦š¸É(12)

o

„Å°œÊεš¸ÉÄ

‡ªµ¤¦o°œ‹µ

r

®oŸ¨·˜£´–”

„Å°œÊεš¸ÉÄ

‡ªµ¤¦o°œ‹µ o°œ

¡Á·Š‡ªµ¤¦

ž¦³­·š›·£µ

®¦º° 100%

Q Q

ker

coo u

o

Å°œÊεš¸Éč

r

Ÿ¨·˜£´–”

K

(12)

¦¼žš¸É 3 „µ¦­¤—»¨‡ªµ¤¦o°œ…°ŠÁ‡¦ºÉ°Š°‰nµÁºÊ°

3.2¤µ˜¦„µ¦š¸ÉčoĜ„µ¦ž¦³®¥´—

‹µ„„µ¦­¤—»¨¡¨´ŠŠµœ‡ªµ¤¦o°œ˜µ¤š·«šµŠ„µ¦Å®¨…°Š‡ªµ¤¦o°œ

š¸É­—ŠÄœ¦¼žš¸É 3 šÎµÄ®oš¦µ™¹Šž¦·¤µ–„µ¦Äo¡¨´ŠŠµœ‡ªµ¤¦o°œ…°Š

Á‡¦ºÉ°Š°‰nµÁºÊ°ÄœÂ˜n¨³­nªœÂ­—ŠŸ¨°¥¼nĜ¦¼žš¸É 4 Ž¹ÉŠ¡ªnµ„µ¦­¼Á­¸¥

‡ªµ¤¦o°œ‹³Á„·—¤µ„š¸É­»—‹µ„„µ¦¦³Á®¥š¸ÉŸ·ªœÊε¦o°œ ‡·—Áž}œ¦o°¥¨³

57.76 …°Š‡ªµ¤¦o°œš¸Éčo ‹µ„œ´Êœ‹¹ŠÅ—o„ε®œ—¤µ˜¦„µ¦š¸ÉčoĜ„µ¦¨—

„µ¦­¼Á­¸¥‹µ„„µ¦™nµ¥ÁšŸnµœŸœ´ŠÂ¨³„µ¦¦³Á®¥…°ŠœÊε¦o°œ—´Šœ¸Ê 1. „µ¦¨—„µ¦­¼Á­¸¥‡ªµ¤¦o°œš¸ÉŸœ´Š™´Š ×¥„µ¦šµ—oª¥­µ¦

nunsulate Ž¹ÉŠ¤¸¨´„¬–³Áž}œŒœªœ­Îµ®¦´šµÁ‡¨º°Ÿ·ªŸœ´Š­Â˜œÁ¨­

—oµœœ°„ ­µ¤µ¦™¨—°»–®£¼¤·š¸ÉŸ·ª­´¤Ÿ´­…°Š™´Š‹µ„Á—·¤ 73 oC Á®¨º°

51oC¨—¨Šž¦³¤µ– 22 oCš´ÊŠœ¸Ê…¹Êœ„´‹Îµœªœ´Êœš¸Éšµ

2.„µ¦¨—„µ¦¦³Á®¥š¸ÉŸ·ªœÊε¦o°œ ×¥„µ¦Äo¨¼„°¨¡¨µ­˜·„œ·—

polycarbonate …œµ—Á­oœŸnµœ«¼œ¥r„¨µŠ£µ¥œ°„ 35 mm. ­Îµ®¦´Äo

¨°¥žd—Ÿ·ª®œoµœÊε¦o°œÄœ¡ºÊœš¸ÉŸ·ªœÊε 4.86 m2 ®¦º°‡·—Áž}œ¦o°¥¨³ 20 …°Š¡ºÊœš¸ÉŸ·ª´ÊœœÊε¦o°œš´ÊŠ®¤—

¦¼žš¸É 4 Sankey diagram ­¤—»¨¡¨´ŠŠµœ„n°œž¦´ž¦»Š

3.2.1 „µ¦ž¦³Á¤·œŸ¨ž¦³®¥´— ‹µ„ž¦·¤µ–‡ªµ¤¦o°œ­¼Á­¸¥š¸É™nµ¥Áš

°°„‹µ„Ÿœ´Š®¨´Š„µ¦šµ—oª¥Œœªœ ¨³°´˜¦µ„µ¦¦³Á®¥…°ŠœÊε¦o°œš¸É

¨—¨Š ×¥œÎµŸ¨š¸Éŗo¤µž¦³Á¤·œŸ¨„µ¦ž¦³®¥´—‹µ„ž¦·¤µ–…°ŠœÊε¤´œ

ÁºÊ°Á¡¨·Š š¸Éčo„´®¤o°Å°œÊεš¸É¨—¨Š ¨³Áš¸¥„´˜oœš»œ…°ŠÁºÊ°Á¡¨·Š

œÊε¤´œÁ˜µÃ—¥°µ«´¥­¤„µ¦š¸É(13)

HHV m Ș Q

f

b loss (13)

×¥š¸É Kb ‡º° ž¦³­·š›·£µ¡…°Š®¤o°Å°œÊε­¤¤˜·Ä®o¤¸‡nµÁšnµ„´ 80%

Qloss ‡º° ž¦·¤µ–‡ªµ¤¦o°œ­¼Á­¸¥š¸É¨—¨Š‹µ„¤µ˜¦„µ¦š¸ÉčoĜ„µ¦

ž¦³®¥´— mf ‡º° ž¦·¤µ–œÊε¤´œÁºÊ°Á¡¨·Š HHV‡º° ‡nµ‡ªµ¤¦o°œ…°Š

ÁºÊ°Á¡¨·Šš¸ÉčoĜ„µ¦Ÿ¨·˜Å°œÊε

Á¤ºÉ°š¦µŸ¨„µ¦ž¦³®¥´—Äœ¦¼žž¦·¤µ–…°ŠÁºÊ°Á¡¨·Š‹µ„­¤„µ¦š¸É 13¨oªœÎµ¤µÁš¸¥„´¦µ‡µ…°ŠœÊε¤´œÁºÊ°Á¡¨·ŠÃ—¥‡Îµœª–˜µ¤­¤„µ¦

š¸É(14)—´Šœ¸Ê

A = mf Cf OP.hr (14) ×¥š¸É A ‡º° ÁŠ·œš¸Éž¦³®¥´—Å—o˜n°že×¥‡·—‹µ„¦µ¥Å—o…°Šž¦·¤µ–

ÁºÊ°Á¡¨·Šš¸É¨—¨ŠCf ‡º° ¦µ‡µ‡nµÁºÊ°Á¡¨·Šš¸ÉčoŸ¨·˜Å°œÊε OP.hr

‡º° ´ÉŠÃ¤ŠšÎµŠµœÄœ¦°že

3.2.2„µ¦ž¦³Á¤·œŸ¨˜°Âšœ„µ¦¨Šš»œ [5] ž¦³Á¤·œ‹µ„¦³¥³Áª¨µ‡ºœ

š»œÂ¨³°´˜¦µŸ¨˜°Âšœ£µ¥Äœ Ÿ¨˜°Âšœ…°Š¤µ˜¦„µ¦˜nµŠ Ç š¸É Á…oµÁ„–”r‡ª¦¤¸¦³¥³Áª¨µ‡ºœš»œš¸É˜É優nµ 7 že ®¦º°¤¸°´˜¦µŸ¨˜°Âšœ

£µ¥Äœ­¼Š„ªnµ 25% ×¥¤¸ª·›¸„µ¦ž¦³Á¤·œ—´Šœ¸Ê

1. ¦³¥³Áª¨µ‡ºœš»œ (payback period, n) Ž¹ÉŠ®µÅ—o‹µ„­¤„µ¦š¸É (15)—´Šœ¸Ê

1 A )n i (1

)n i (1 P i

(15)

„µ¦ž¦³»¤ª·µ„µ¦Á‡¦º°…nµ¥ª·«ª„¦¦¤Á‡¦ºÉ°Š„¨Â®nŠž¦³Áš«Åš¥‡¦´ÊŠš¸É 20 18-20 ˜»¨µ‡¤ 2549 ‹´Š®ª´—œ‡¦¦µ­¸¤µ

Suranaree University of Technology

ETM041

18-20 October 2006 , Mandarin Golden Valley Hotel & Resort Khao Yai , Nakhon Ratchasima

(5)

×¥š¸É P‡º° ÁŠ·œ¨Šš»œ n ‡º° ¦³¥³Áª¨µ‡ºœš»œ i ‡º° °´˜¦µ—°„Á¸Ê¥

­¤¤˜·Ášnµ„´ 12.5 % ˜n°že

2. °´˜¦µŸ¨˜°Âšœ£µ¥Äœ (internal rate of return, IRR)

0 1 P

t [1 IRR]t

A -

N

¦

(16) ×¥š¸É t‡º° žeš¸É¡·‹µ¦–µ N‡º° °µ¥»„µ¦ÄoŠµœ°»ž„¦–r IRR ‡º°

°´˜¦µŸ¨˜°Âšœ£µ¥Äœ (¦o°¥¨³) 4. Ÿ¨„µ¦ª·Á‡¦µ³®r

4.1 „µ¦¨—„µ¦­¼Á­¸¥‡ªµ¤¦o°œš¸ÉŸœ´Š™´Š

„µ¦Äo­µ¦ nunsulate Ž¹ÉŠÁž}œª´­—»ž¦³Á£šŒœªœ‡ªµ¤¦o°œÄošµ Á‡¨º°Ÿ·ª…°ŠÁ‡¦ºÉ°Š°‰nµÁºÊ° šÎµÄ®o°»–®£¼¤·…°ŠŸœ´Š¨—¨Š‹µ„Á—·¤

73oCÁ®¨º° 51 oCšÎµÄ®oŸ¨˜nµŠ…°Š°»–®£¼¤·Ÿ·ªŸœ´Š„´°»–®£¼¤·

ª—¨o°¤¨—¨ŠÂ¨³ž¦³Á¤·œ„µ¦­¼Á­¸¥‡ªµ¤¦o°œÃ—¥°µ«´¥Ÿ¨˜nµŠ…°Š

°»–®£¼¤·—´Š„¨nµª¡ªnµ­µ¤µ¦™¨—„µ¦­¼Á­¸¥‡ªµ¤¦o°œÅ—o 7,373 kJ/hr

®¦º°¦o°¥¨³ 64.2 Á¤ºÉ°Áš¸¥„´„n°œž¦´ž¦»Š ‡·—Áž}œž¦·¤µ–œÊε¤´œ

ÁºÊ°Á¡¨·Šš¸Éž¦³®¥´—Å—oÁšnµ„´ 0.213 ¨·˜¦/´ÉªÃ¤Š ×¥¤¸ÁŠ·œ¨Šš»œ 3,040

µš ‡·—Áž}œÁŠ·œš¸Éž¦³®¥´—Å—o 6,652 µš/že °µ¥»ÄoŠµœ„ε®œ—š¸É 5 že

Ÿ¨˜°Âšœ„µ¦¨Šš»œ…°Š¤µ˜¦„µ¦ 218 % ¦³¥³Áª¨µ‡ºœš»œ 0.5 že 4.2 „µ¦¨—„µ¦¦³Á®¥š¸ÉŸ·ªœÊε¦o°œ

×¥„µ¦Äo¨¼„°¨š¦Š„¨¤¨°¥žd—Ÿ·ª®œoµ…°ŠœÊε¦o°œÄœ¡ºÊœš¸ÉŸ·ª 4.86 m2 ­µ¤µ¦™„µ¦­¼Á­¸¥‡ªµ¤¦o°œÅ—o‹µ„„µ¦¦³Á®¥š¸ÉŸ·ª®œoµœÊε

¦o°œÅ—o 33,984 kJ/hr ®¦º°¦o°¥¨³ 25.54 Á¤ºÉ°Áš¸¥„´„n°œž¦´ž¦»Š

‡·—Áž}œž¦·¤µ–œÊε¤´œÁºÊ°Á¡¨·Šš¸Éž¦³®¥´—Å—oÁšnµ„´ 1.07 ¨·˜¦/´ÉªÃ¤Š

×¥¤¸ÁŠ·œ¨Šš»œÄœ„µ¦—εÁœ·œ„µ¦¤µ˜¦„µ¦œ¸Ê 35,200 µš ‡·—Áž}œÁŠ·œ

‡nµÁºÊ°Á¡¨·Šš¸Éž¦³®¥´—Å—oÁšnµ„´ 29,606 µš/že °µ¥»ÄoŠµœ„ε®œ—š¸É 5že Ÿ¨˜°Âšœ„µ¦¨Šš»œ…°Š¤µ˜¦„µ¦ 91.82 % ¦³¥³Áª¨µ‡ºœš»œ

1.19že

Ÿ¨„µ¦¨—„µ¦­¼Á­¸¥‡ªµ¤¦o°œ®¨´Šž¦´ž¦»ŠÃ—¥¤µ˜¦„µ¦š´ÊŠ­°Š

­—Š°¥¼nĜ¦¼žš¸É 5

¦¼žš¸É 5 Sankey diagram ­¤—»¨¡¨´ŠŠµœ®¨´Šž¦´ž¦»Š

5.­¦»ž

„µ¦ª·Á‡¦µ³®r¡ªnµ­£µ¡Á—·¤Á‡¦ºÉ°Š‹´„¦š¸Éčo¤¸„µ¦­¼Á­¸¥‡ªµ¤

¦o°œÁ„·—…¹Êœ¤µ„ ­µÁ®˜»‹µ„„µ¦°°„Ã‡¦Š­¦oµŠÁ—·¤š¸É¤¸‹»—°n°œš¸É˜o°Š

„oŅ ¨³‹µ„¤µ˜¦„µ¦š´ÊŠ­°Šš¸ÉÁ¨º°„čo¡ªnµ­µ¤µ¦™ž¦³®¥´—Å°œÊε Ĝ„¦³ªœ„µ¦Ÿ¨·˜Å—o 17.96% ‡·—Áž}œ‡nµÁºÊ°Á¡¨·Šš¸Éž¦³®¥´—Å—o Ášnµ„´ 36,258 µš/že ®¨´Š„µ¦ž¦´ž¦»Šž¦³­·š›·£µ¡…°ŠÁ‡¦ºÉ°Š

Á¡·É¤…¹ÊœÁž}œ 44.41% ¨³š´ÊŠ­°Š¤µ˜¦„µ¦œ¸Ê¤¸¦³¥³Áª¨µ„µ¦‡ºœš»œ­´Êœ

¨³Ä®oŸ¨˜°Âšœ­¼Š ×¥¥´Š¤¸Ã°„µ­š¸É‹³…¥µ¥Ÿ¨š¸É‹³œÎµÅžÄo„´

Á‡¦ºÉ°Š°‰nµÁºÊ°Á‡¦ºÉ°Š°ºÉœ š¸Éčo°¥¼n£µ¥ÄœÃ¦ŠŠµœ®¦º°Á‡¦ºÉ°Š‹´„¦ž¦³Á£š

°ºÉœ Ç š¸É¤¸¨´„¬–³„µ¦ÄoŠµœÄ„¨oÁ‡¸¥Š„´œ

6.„·˜˜·„¦¦¤ž¦³„µ«

ǦŠ„µ¦œ¸Êŗo¦´š»œ°»—®œ»œ‹µ„ ­Îµœ´„Šµœ„°Šš»œ­œ´­œ»œ„µ¦

ª·‹´¥ (­„ª.)  iµ¥°»˜­µ®„¦¦¤ ž¦³‹Îµže 2548 7.Á°„­µ¦°oµŠ°·Š

[1] °£·¦´„¬r ­ª´­—·Í„·‹ ¨³‹»¨¨³¡Š«r ‹»¨¨³Ã¡›· “„µ¦ž¦³®¥´—Å°œÊε Ĝ把µœ¥µ­¼” ªµ¦­µ¦ª·«ª„¦¦¤­µ¦Œ´ª·‹´¥Â¨³¡´•œµ žeš¸É 11Œ´š¸É 1 ¡.«.2543®œoµ 95-103

[2] °£·¦´„¬r ­ª´­—·Í„·‹ ¨³‡–³, 2548, "„µ¦ž¦³®¥´—Å°œÊεĜ

„¦³ªœ„µ¦Ÿ¨·˜Ÿ¨Å¤o„¦³žl°Š", „µ¦ž¦³»¤Á‡¦º°…nµ¥

ª·«ª„¦¦¤Á‡¦ºÉ°Š„¨Â®nŠž¦³Áš«Åš¥ ‡¦´ÊŠš¸É 19, 19-21 ˜»¨µ‡¤

2548,æŠÂ¦¤Á—°³¦°¥´¨¡µ¦µÅ—­r,‹.£¼Á„Ș ®œoµ 803-808 [3] W.C.Turner, Energy Management Handbook, Aee Publication

1993, pp. 180-185

[4] J.P.holman, Heat Transfer, Mc.Graw-hill , 1992 pp 342-350 [5] Reay, D.A., Industrial Energy Conservation , Pergamon, 1979

pp 315-327

„µ¦ž¦³»¤ª·µ„µ¦Á‡¦º°…nµ¥ª·«ª„¦¦¤Á‡¦ºÉ°Š„¨Â®nŠž¦³Áš«Åš¥‡¦´ÊŠš¸É 20 18-20 ˜»¨µ‡¤ 2549 ‹´Š®ª´—œ‡¦¦µ­¸¤µ ETM041

Referensi

Dokumen terkait

"DESIGNING AN ENGLISH TEACHING MATERIAL FOR TENTH GRADE STUDENTS OF CULINARY STUDY PROGRAM", Journal of English Education Program, 2020 Publication "Cross Reality and Data Science