1547845440-The_Ricci_Flow_-_Techniques_and_Applications_-_Part_III__Chow_

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  1. CONSTRUCTION OF THE PARAMETRIX FOR THE HEAT KERNEL 223


in the second line)

(23.29)

ofo: (DxHN) (x, t; y, u)


e k
=LL coeff ·o{o~E (x, t; y, u) a:-p (b.x</>N (x, y)) a:-q ( (t - u)N)
q=O p=O
= E (x, t; y, u) (t - u)N-k-^2 £ Fk,£ (x, y, t - u)

= ( 4 )-n/2 (t _ )N-(n/2)-k-2£ ( d


2
1f u exp (x, Y)) D ( t _ )
4 (t-u) rk,£ x,y, u

for N > ~ + k + 2£, where


Fk,£ E C^00 ( ( (U x M) n Minj(g)) x [O, oo)).


The power N - (n/2) - k-2£ oft - u in (23.29) is due to the fact that each


space derivative of E introduces a (t - u)-^1 factor and each time derivative


of E introduces a (t - u)-^2 or (t - u)-^1 factor. (Recall that d^2 and </>N are


both C^00 functions on Minj(g).)
Given TE (0, oo), let

(23.30) lR.f = { (t, u) E JR.^2 : 0 < t - u ST} C JR;.


In particular, formula (23.29) implies that for any k, .e E NU{O}, any compact
subset K c U, and any T E (0, oo ), we have


(23.31)

Jaf a: (DxHN) I (x, t; y, u) s c (t - u)N-(n/^2 )-k-^2 £ exp (


S C (t _ u)N-(n/2)-k-2£

d^2 (x,y))
4 (t - u)

for all (x, t; y, u) E ( (K x M) n Minj(g)) x lR.f. Note that as a special case
(when k = .e = 0), we have (23.28).
The same types of formulas as (23.29) and (23.31) are true on all of
Minj(g) x lR.f, for any T E (0, oo ), with the partial derivatives 8~ replaced
by covariant derivatives 'V~.


LEMMA 23.10 (Covariant derivatives of heat operator of HN)· For any
k,£ENU{O} and TE (O,oo),


(23.32) Jof'V~ (DxHN) J S C (t - u)N-(n/^2 )-k-^2 £ exp (-:~t(~ ~)

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